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Sulphur-cured rubber particle surface activation and/or devulcanisation process

IPC classes for russian patent Sulphur-cured rubber particle surface activation and/or devulcanisation process (RU 2354671):
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Biodegradable granular polyolefin blend represents antimisting granules sized 2-8 mm of apparent bulk density 530-630 kg/m3, granule density less than 920-1300 kg/m3. Herewith melt flow index (MFI) of the parent polyolefin is MFI=2.5-25.0 g/10 minutes. Processing and relevant aid concentrate contains at least one biodegradable additive, thermostabilisers, antioxidants, lubricants, antistatic aids, pigments, fillers etc. The granular polymer blend is produced within a number of stages to ensure uniform distribution of all the aids in polyolefin. Four powder material flows are used. Three aid compositions are mixed with three parts of parent powder polyolefin in ratio 1:4, 1:3 and 1:2 respectively. Prepared concentrate mother stocks are supplied to the fourth combined mixer with residual part of polyolefin. If required, necessary liquid biodegradable additive. The blend is stirred and homogenised at 150-250°C.

FIELD: chemistry.

SUBSTANCE: destruction of sulphur bridges and recovery of sulphur is ensured by bioprocessing of rubber particles in a medium containing mesophilous, anaerobic and/or mesophilous, optionally anaerobic and/or mesophilous microaerophilic bacteria and/or one or more enzyme system of the specified bacteria in environment appropriate for the specified bacteria living.

EFFECT: improved vulcanisation ability of processed rubber particles, and better quality of rubber products provided.

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The present invention relates to a method of activating and/or devulcanization of the surface of the particles of the rubber material vulcanized grey.

In patent publications DE 4425049 C1, DE 19607281 A1 and US 5,506,283 describes the different ways to activate crushed scraps of old rubber and rubber waste. These methods are based on the principles of either a physical or a chemical treatment or a combination of these principles is processing.

In addition, in patents DE 4042009 C2, EP 0493732 B1, US 5,597,851 and DE 19728036 A1 describes how the activation of powdered or granulated rubber under the action of microorganisms and enzymes.

In patents DE 4042009 C2 and EP 0493732 B1 describes a method based on microbial oxidation of polysulfide sulfur associated with the vulcanization of rubber. Oxidation of polysulfide sulfur on the surface of the particles of the rubber material occurs under the action of chemolithotrophic microorganisms bacterial suspension at a given oxygen flow. These bacteria belong to the species Thiobacillus. The oxidation of sulfur is usually produced prior to the formation of sulfate. The final product of the method is a re-plasticized (replasticized) rubber material with a low sulfur content and a good break.

A similar method is described in patent US 5,597,851. The feature of this method is that, on the one hand, as oxidizing sulfur microorganism used, mainly thermophilic and possibly chemolithotrophic species Sulfolobus acidocaldarius, and on the other hand, the treatment of the particles of the rubber material is produced simply by using the enzyme systems of the specified microorganism. Particles themselves of the rubber material are not in direct contact with microorganisms.

In the application DE 19728036 A1 describes a method in which the surface of the particles of the rubber material to form a specific reactive functional groups such as hydroxyl, epoxy groups and carboxyl groups formed by the biotechnological processing of particles of vulcanized rubber material for a given reaction time/duration of oxidation. The result is the ability to vulcanized powdered activated granulated rubber and rubber, various plastics (plastics), bitumens and other polymers. In microbial oxidation also participate bacteria species Thiobacillus.

Previously known methods of microbial activation powder granulated rubber and rubber, conducted by the oxidation of sulphur, has the following serious drawbacks:

1. These activation methods based on the oxidation. In addition to the required oxidation of polysulfide sulfur is both inevitable undesired oxidation on kernich chain (accession free radicals). While on the surface of the particles virtually no capable of binding sites. The degree of decomposition, among others, influenced by the following factors: the type of rubber material (number of double bonds), the reaction temperature and the concentration of oxygen dissolved in the suspension.

2. Among other things, the destruction of the polymer chains leads to undesirable allocation of specific components of the rubber material (plasticizers, carbon black, zinc oxide and so on).

3. To avoid contamination with foreign substances ways must be carried out at very low pH values (from 1 to 3), which imposes additional restrictions on the material of the bioreactors, and improves the quality requirements for wastewater handling.

These drawbacks can be eliminated when using anaerobic methods. Such methods are described Bredberg (.Bredberg, J.Perssom, M.Christiansson, .Stenberg, .Hoist: "Anaerobic desulphurization of ground rubber with thermophilic archaeon Pyrococcus furiosis - a new method for rubber recycling", journal of Appl. Environ. Biotechnol. (2001), 55, p.43-48); they are under the influence of reducing sulfur anaerobic hyperthermophilic archaebacteria (archaeon) Pyrococcus furiosis. However, this method has several disadvantages, in particular that associated with hyperthermophilic characteristics of archaebacteria:

1. Processing of powdered rubber for d is sustained fashion period of time at temperatures of 90-100°C leads to the destruction of the polymer chains of the elastomer and, thus, deterioration of the most important technical characteristics of the material (tensile strength, elongation at break, abrasion and so on).

2. Under the high temperature of the powdery rubber allocated additives (plasticizers, carbon black, zinc oxide, chemical protective equipment, etc. that make the microorganisms and, therefore, impede the flow of flue or lead to complete stoppage.

3. The implementation of the method in the range such high temperatures uneconomical from the point of view of large-scale production, but also impractical from an environmental point of view (the dumping of toxic materials in waste water production).

Thus, the present invention is to provide a method of activating and/or devulcanization of the surface of the particles of the rubber material vulcanized grey, which could be carried out at temperatures essentially below 90°C and which would not have the above disadvantages inherent in the methods microbial oxidation.

The problem is solved by the method proposed in accordance with the present invention and having the characteristics specified in claim 1 of the claims. Improvements and examples of implementation of the method specified in the claims dependent on claim 1.

In accordance with the present invention, a method of activating and/or devulcanization of the surface of the particles of the rubber material vulcanized grey, with which to destroy the sulfur bridges and for recovery of sulfur particles of the rubber material is subjected to biotechnological processing in an environment containing mesophilic anaerobic and/or mesophilic, perhaps, anaerobic and/or mesophilic microaerophilic bacteria and/or one or more enzymatic system of these bacteria. The notion of “possible, anaerobic bacteria” in the present description refers to bacteria that can exist both in the presence and in the absence of oxygen.

A significant difference of this method from the method described Bredberg, is the use of mesophilic microorganisms. Optimal for the existence of mesophilic bacteria, the temperature is from 20 to 45°C. Thus, the method proposed in accordance with the present invention, is carried out at temperatures that are significantly below 90°C. Thus, it is possible to avoid or at least substantially reduce the above drawbacks inherent to the processing of hyperthermophilic microorganisms. Because the bacteria used for implementing the method, proposed in accordance with the present invention, in addition, are anaerobic and/or possibly anaerobic and/or microaerophilic bacteria, the method can be carried out in the absence of oxygen or in the presence of very small quantities. To eliminate the foregoing disadvantages inherent in the methods, which are based on microbial oxidation.

The fundamental principle at the basis of the method of processing particles of rubber material in accordance with the present invention, is that the microorganisms destroy the sulfur bridges in volcanoserver.com rubber material on the particle surface and partially or fully restore sulfur, without destroying it, thus, the polymer chains of the elastomer. Using the method proposed in accordance with the present invention, receive activated particles of rubber material, compared to the inactivated particles of rubber material, they have an increased ability to vulcanization. Thus, using such activated particles of rubber material, in particular in the form of powder granulated rubber and rubber, it is possible to obtain high-quality products.

According to the present invention the particles of the rubber material is subjected to microbial and/or enzymatic treatment. In the case of enzymatic treatment, in particular treatment is carried out, the claim is uchitelle using enzyme system of bacteria (set of enzymes which contain bacteria), preferably isolated from these bacteria.

The term “microbial processing” understand that the bacteria are in contact (interact) with the surface of the rubber particles. However, the enzymatic processing of the processing itself, i.e. the destruction of the sulfur bridges and/or recovery of sulfur occurs under the action of only enzyme system or enzyme systems of bacteria.

More specifically, the enzyme treatment may be performed as follows: first, bacteria are grown in primary culture in the absence of contact with the treated particles of the rubber material vulcanized grey, on the other sulfur substrate, for example, in the presence of elemental sulfur. Then the bacteria are subjected to decomposition, and the enzyme system allocate (collect) the well-known ways. This is followed by a treatment of the particles of the rubber material vulcanized grey, exclusively through selected enzyme system.

However, the method can be carried out in the case, when the selection of the enzyme system by bacteria occurs in situ, i.e. the enzyme system required for enzymatic processing, not pre-allocate.

It is advantageous if the processing environment for particles of rubber material contains water, nutrients, carbon source and bacteria or consists of the shown ingredients ie is a suspension. According to the preferred implementation of the method the concentration of the particles of the rubber material in the environment support essentially below 35 wt.%. Higher concentrations of particles of rubber material cause problems, such as complicated mixing of the reaction mass, the mass transfer and the growth of bacteria, for example, due to the higher concentration of toxic chemicals, including antioxidants.

Additionally, to reduce temperature gradients and/or concentration gradients can be mixing environment. Preferably the mixing is made very carefully, for example, by means of stirrers.

Another suitable example of the method proposed in accordance with the present invention is the treatment of anaerobic or microaerophilic conditions. In addition, in accordance with the present invention it is possible to carry out processing, essentially, at temperatures below 90°C., in particular below 50°C, preferably within the temperature range that is optimal for mesophilic bacteria, which is approximately from 20 to 45°C. Preferably the treatment is carried out at temperatures in the range from 33 to 37°C.

In the processing of rubber particles of material in General, the production of the t in terms optimally suitable for the existence of mesophilic anaerobic and/or mesophilic, perhaps, anaerobic and/or mesophilic microaerophilic bacteria. In addition, using this method virtually eliminates the above disadvantages of the known methods.

In accordance with the developed method pH range from 5 to 9, in particular from 6 to 8. In addition, the residence time of the particles of the rubber material may be in the range from 4 to 8 days, in particular from 5 to 7 days, preferably approximately 6 days.

The desulfurization produce successfully and optimally, in particular, observing the following parameters and conditions of implementation method:

Temperature treatment: From 33 to 37°C
PH-value: From 6 to 8
The mixing mode: Careful mixing
The average length of stay: 6 days
The particle size of the rubber material: from 0.2 to 0.4 mm

In accordance with an advanced example of the method, the pre is proposed in accordance with the present invention, the bacteria used in the environment and/or to highlight the enzyme systems are bacteria that can use sulfur in the respiratory chain, is able to recover sulfur.

During the tests, it was found that, in accordance with the corresponding phase of adaptation of various anaerobic or perhaps anaerobic or microaerophilic mesophilic bacteria able to destroy the sulfur bridges in vulcanized rubber and recover sulfur. Among other bacteria positive results were obtained with bacteria Desulfuromonas thiophila, Desulfuromonas palmitatis, Sulfurospirillum deleyianum and Desulfuromonas acetoxidans. Therefore, it is reasonable to use bacteria that essentially belong to one of these strains. In addition, all or some of the bacteria may belong to mixed populations.

Very good speed desulphurization were obtained using anaerobic mesophilic mixed populations in which in addition to reducing sulfur bacteria are significant quantities of methane-producing bacteria. This population was isolated from sediment of the river Saale; it is particularly resistant.

As for the particles of the rubber material, one example implementation of the present invention essentially provides processing of rubber powder and/and and powdered rubber and/or granulated rubber. Under the rubber powder and powdered rubber imply material with a particle size less than 1 mm, and under the granulated rubber understand the material with particle size in the range from about 1 mm to 5 mm, it is Advisable and advantageous if the size of the treated particles of the rubber material is in the range from 0.1 to 0.6 mm, in particular from 0.2 to 0.4 mm, i.e. if rubber is a powdery rubber and rubber powder.

In accordance with an advanced example implementation of the present invention, it is expedient if the treated particles of rubber material, essentially represent the particles of the rubber material is made of rubber, vulcanized grey, or composites based on rubber, vulcanized grey. The method proposed in accordance with the present invention, especially suitable for surface activation and/or devulcanization of all types of rubber, vulcanized grey, for example, SBA (styrene-butadiene elastomer, SBR), NK (natural rubber, NR), NRE (Acrylonitrile-butadiene elastomer, nitrile rubber, NBR), APD (ethylene-propylene-diene elastomer, EPDM).

In accordance with an advanced example implementation of the present invention the particles of the rubber material is obtained from scraps of old rubber (such as tires, of which the men of technical rubber, such as sealing material, pieces, castings, rubber, conveyor belts) and/or rubber waste (industrial waste rubber manufacture or production of rubber processing). Thus, the method proposed in accordance with the present invention, is used for the disposal of scraps of old rubber and/or rubber waste.

In accordance with another example implementation of the treated particles of the rubber material was obtained during grinding, in particular when Stripping (Stripping), and/or hot grinding, and/or cold grinding, and/or cryogenic grinding, and/or wet grinding. Particularly preferably, if the temperature during the grinding of the material to obtain particles of rubber material remains so low, in particular significantly less than 90°With that essentially does not occur thermal-oxidative decomposition of the particles of the rubber material.

In accordance with a particularly preferred example of the method according to the present invention, surface activation and/or devulcanization practically limit the surface of the particles of the rubber material and/or layers that are close to the surface, so as not to modify the material properties in the bulk of the specified particles. At this layer, located close to the surface, has a thickness of not bol is e 300. This means that the effect of mesophilic desulphurization deliberately limit the surface of the particle and/or layers that are close to the surface.

Appropriate processing of the rubber particles of the material to be produced in the bioreactor. The bioreactor is a device for processing materials using microorganisms in a reproducible and controlled manner. In addition, it may be made continuous or quasi-continuous, or periodic loading of the treated particles of the rubber material in the bioreactor, as well as continuous or quasi-continuous, or periodic discharge of treated rubber particles of material from the bioreactor. Alternatively, or additionally, the reactor can be operated in such a way that the discharge of treated rubber particles of material from the bioreactor carried out in the absence or with very little loss of bacteria and/or enzymatic environment for processing particles of rubber material, and/or when there is no contact or by contact of a very small number of bacteria and/or enzymatic environment with atmospheric oxygen. This effect reached by precipitation and subsequent separation of the particles of the rubber material under anaerobic conditions.

It is advisable, if you implement the method of the sulfur bridges contained in the rubber particles mater is Ala, at least partially destroyed during processing, and sulfur passes into one or more gaseous reaction products. One of the gaseous products of the reaction may be hydrogen sulfide. In a particularly advantageous example of the implementation of the hydrogen sulfide, which is formed during processing of the rubber particles of the material, remove the continuous or quasi-continuous manner from the gas phase. In the result, it is possible to prevent the slowdown in activity and/or poisoning bacteria.

In an example implementation of the method proposed in accordance with the present invention, the treated rubber particles of the material after treatment is washed with water, in particular, to reduce the salt content, and then thoroughly dried, in particular, essentially, at temperatures below 90°C.

In yet another example implementation of the obtained particles of rubber material, the surface of which is activated by using the above-described processing, in particular powdered rubber, and then used for the manufacture of rubber products. In connection with these new rubber products can be made either from particles of a rubber material having a surface activated using the above-described processing, any of the particles of a rubber material having an activated surface, mixed with fresh rubber, cast the STI, using chemical vulcanization.

Further, in accordance with the present invention the obtained particles of rubber material with an activated surface, in particular powdered rubber, can be used for the manufacture of elastomeric alloys, in particular, by using the phase interaction with plastics (plastics), preferably polypropylene (PP) and/or polyurethane (PU).

In addition to the improvement of the material properties of rubber products manufactured by the above method, the use of such particles of the rubber material with the activated surface also leads to a reduction of certain positions in the cost of products.

For example, the use of powdered scraps of old rubber, activated by the method proposed in accordance with the present invention, in combination with fresh rubber, leads to a significant improvement of material-technical parameters of the obtained product, in particular a deformation, elongation at tear resistance and tensile impact. In addition, it can be shown that the combination of powdered activated scraps of old rubber and powder APDA rubber with thermoplastische (thermoplastics), in particular polypropylene, receive materials, physical and mechanical properties that are close to the corresponding feature is intikam thermoplastic elastomers. In particular, improves elasticity in comparison with elasticity similar products made from powdered raw scraps of old rubber. This indicates a course of intensive mutual diffusion of polymer chains phase and an elastomeric phase and possibly also on the chemical cure of these two phases (intensive phase interaction).

Hereinafter the present invention will be illustrated with one example implementation.

Ground cryogenic way powder APDA rubber particles which have a size of less than 0.4 mm, was subjected to microbial surface activation in anaerobic conditions. After the activation period lasts for 8 days level of desulphurization rubber was approximately 4%. Then powdered rubber, activated by microbial method, and Deaktivierung powdered rubber of the same original sample, respectively, mixed with fresh, APDA rubber in the ratio of 1:1 and subjected to vulcanization.

The following table shows the values of tensile strength and relative elongation at break, measured for the respective products and for fresh, APDA rubber, taken as reference sample.

The final cured product is received: The tensile strength, MPa Elongation at break, %
APDA - fresh rubber (without admixture of powdered rubber) 28 595
50% of APDA - fresh rubber + 50% powdered activated rubber 25 555
50% of APDA - fresh rubber + 50% non-activated powdered rubber of 17.5 385

Comparison of the specified values of important physical and mechanical properties such as tensile strength and elongation at break, shows that treatment of the particles of the rubber material in accordance with the present invention, i.e. in particular, in the above example, microbial activation of powdered rubber, carried out under anaerobic conditions leads to a significant improvement of the material properties compared to materials, including raw particles of rubber material.

Thus, in General, activated rubber particles of the material treated in accordance with the method proposed by the present invention, have shown an increased ability to vulcanizes and compared to untreated particles of rubber material, that enables us to produce the best quality products.

1. The activation method and/or devulcanization of the surface of the particles of the rubber material vulcanized grey, with which to destroy the sulfur bridges and for recovery of sulfur particles of the rubber material is subjected to biotechnological processing in an environment containing mesophilic anaerobic and/or mesophilic, facultative anaerobic and/or mesophilic microaerophilic bacteria and/or one or more enzyme system of these bacteria, under conditions suitable for the existence of these bacteria.

2. The method according to claim 1, in which the treatment of the particles of the rubber material to produce microbial and/or enzymatic method, in particular, exclusively using enzyme system, preferably selected from bacteria.

3. The method according to claim 1, in which the environment for the processing of the particles of the rubber material contains water, nutrients, carbon source and bacteria, or consists of these ingredients.

4. The method according to claim 1, in which the concentration of the particles of the rubber material in the environment support below 35 wt.%.

5. The method according to claim 1, wherein to reduce temperature gradients and/or gradients of concentration of the medium is stirred, in particular, are thoroughly mixed, preferably using a mixer.

6. The method according to claim 1, which is the processing carried out in anaerobic or microaerophilic conditions.

7. The method according to claim 1, in which the treatment is carried out at temperatures below 90°C., in particular below 50°C, preferably within the temperature range that is optimal for mesophilic bacteria, in particular in the range from 33 to 37°C.

8. The method according to claim 1, in which the treatment is carried out at pH values in the range from 5 to 9, in particular from 6 to 8.

9. The method according to claim 1, wherein the residence time of the particles of the rubber material in the environment is from 4 to 8 days, in particular from 5 to 7 days, preferably approximately 6 days.

10. The method according to claim 1, in which bacteria represent or include bacteria, is able to "breathe" sulfur, is able to recover sulfur, and, in particular, bacteria belonging to one or more of the following bacterial strains: Desulfuromonas thiophila, Desulfuromonas palmitatis, Sulfurospirillum deleyianum and Desulfuromonas acetoxidans.

11. The method according to claim 1, in which bacteria represent or include mixed populations.

12. The method according to any one of claims 1 to 11, in which the treated rubber particles of the material are or include rubber powder and/or powdered rubber and/or granulated rubber, and the size of the particles preferably is in the range from 0.1 to 0.6 mm, in particular from 0.2 to 0.4 mm

13. The method according to any one of claims 1 to 11, in which the treated rubber particles of the material are a sludge which include particles of rubber material, made of rubber, vulcanized grey, or composites based on rubber, vulcanized grey.

14. The method according to any one of claims 1 to 11, in which the treated rubber particles of the material are or include particles of rubber material made from scraps of old rubber and/or rubber waste, and the method, thus, provides for the disposal of scraps of old rubber and/or rubber waste.

15. The method according to any one of claims 1 to 11, in which the treated particles of the rubber material was obtained during grinding, in particular when Stripping (Stripping) and/or hot grinding, and/or cold grinding, and/or cryogenic grinding, and/or wet grinding; in this case, preferably, the temperature of the particles of the rubber material is so low, in particular significantly below 90°C, which essentially does not occur thermal-oxidative decomposition of the particles of the rubber material.

16. The method according to any one of claims 1 to 11, in which the activation and/or devulcanization surface practically limit the surface of the particles of the rubber material and/or layers that are close to the surface, in particular, of a thickness of not more than 300 nm, in order not to modify the material properties in the bulk of the particles of the rubber material.

17. The method according to any one of claims 1 to 11, in which the treatment of the particles of the rubber material p is izvodyat in the bioreactor.

18. The method according to 17, in which the loading of the treated particles of the rubber material in the bioreactor and/or unloading of the processed particles of the rubber material from the bioreactor continuously or quasi-continuous or periodic manner, and/or the reactor operates so that when the discharge of treated rubber particles of material from the bioreactor is only a very small leakage of bacteria and/or enzymatic environment for processing particles of rubber material, or such leakage does not occur, and/or only a small number of bacteria and/or enzymatic environment in contact with atmospheric oxygen, or such contact is completely absent, which carried out, in particular by precipitation and subsequent separation of the particles of the rubber material under anaerobic conditions.

19. The method according to any one of claims 1 to 11, in which the gaseous products resulting from at least partial destruction of the sulfur bridges remove continuous or quasi-continuous manner from the gas phase.

20. The method according to any one of claims 1 to 10, in which the treated rubber particles of the material after treatment is washed with water, in particular, to reduce the salt content, and then thoroughly dried, in particular, at temperatures below 90°C.

21. The method of obtaining rubber from the rubber particles mA is Arial, activated by the method according to any one of claims 1 to 20.

22. The method according to item 21, in which products are produced only from particles of a rubber material having a surface activated by the method according to any one of claims 1 to 20, or from particles of a rubber material having an activated surface, mixed with fresh rubber.

23. The method of obtaining elastomeric alloys, in particular, by using the phase interaction with plastics (plastics), preferably polypropylene (PP) and/or polyurethane (PU) rubber particles of the material treated by the method according to any one of claims 1 to 20.

 

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