method for recycling a scrap rubber, in particular tires, black carbon powder derived from scrap rub

专利摘要:
METHOD FOR RECYCLING SCRAP RUBBER, IN PARTICULAR, TIRES, BLACK CARBON POWDER DERIVED FROM SCRAP RUBBER, BLACK CARBON GRAIN DERIVED FROM SCRAP RUBBER, BLACK CARBON POWDER DERIVED FROM SCRAP RUBBER, USAGE BLACK CARBON DERIVED FROM SCRAP RUBBER, E, RUBBER COMPOSITION. The present invention relates to a method for recycling scrap rubber comprising the steps of pyrolysis of scrap rubber to obtain a coal material and grinding the coal material thus obtained. The present invention also relates to carbon black powders and carbon black granules obtained by the method according to the invention. Furthermore, the present invention relates to the use of said carbon black powder and compositions comprising said carbon black powders.
公开号:BR112014014978B1
申请号:R112014014978-0
申请日:2012-12-21
公开日:2021-05-11
发明作者:Arnoldus Henricus Adrianus Verberne；Jan Anne Jonkman；Christopher Michael Twigg
申请人:Black Bear Carbon B.V.；
IPC主号:

专利说明:

HISTORY OF THE INVENTION
[001] The present invention relates to a method for recycling scrap rubber comprising the steps of pyrolysis of scrap rubber to obtain a coal material and grinding the coal material thus obtained. The present invention also relates to carbon black powders and carbon black granules obtained by the method according to the invention. Furthermore, the present invention relates to the use of said carbon black powder and compositions comprising said carbon black powders.
[002] Tire recycling or rubber recycling is the process of recycling tires (usually vehicle tyres) that are no longer suitable for use on vehicles, due to wear or irreparable damage (such as punctures). These tires are also known as ‘End of Life’ (ELT) tires. These tires are among the largest and most problematic waste sources due to the large volume produced and their durability.
[003] Rubber tires used from sources such as automobiles and trucks include materials that, if successfully recycled, can be used for a wide variety of industrial uses. Extending the service life of materials in these tires is an area of intense interest, in particular, in the implementation of cradle-to-cradle products in the tire industry.
[004] Tire recycling is, however, a difficult and costly process and, as a result, millions of tires per year are worn out and accumulated, usually at landfill sites. Scrap tires are bulky and consume a significant amount of space, even if compacted. Furthermore, these used tires also cause air pollution if burned.
[005] A known way to recycle tires is through pyrolysis. Pyrolysis uses heat in the absence of oxygen to break down the tire to produce steel, volatile gases and carbonaceous residues. Carbonaceous carbon material is rich in black carbon, which can be used for many applications.
[006] However, an economically viable way to reprocess scrap tires into valuable final materials is not known. Examples of valuable products into which black carbon powder derived from scrap rubber could be compounded include car and light truck tires, shoe soles and heels, conveyor belts, car and household carpets, brake and clutch pads, V-belts , floor, cable insulation, hoses.
[007] Currently, black carbon powder derived from scrap tires has several problems associated with it, for example a high volatile content prevents prior art black carbon from being ground to a particle size of less than 40 microns. This is because high amounts of volatiles reduce the availability of coal to be ground. In the art, a coal material with a high volatile content is known as 'brittle'. This so-called brittle state is an important factor in determining the grinding capacity of a material, thus making the coal material progressively less susceptible to grinding as the volatile content increases. Thus, this black carbon cannot be added to said valuable products.
[008] Document US5037628 discloses a pyrolysis method for recovering carbonaceous materials from scrap tires by pyrolysis of scrap tires in a pyrolysis step process to form a coal material.
[009] The document US2002119089 describes a one-stage process for pyrolysis of scrap tires involving the use of a rotating drill. The carbon black product has an average particle size of 0.125mm, making the product suitable for low-grade applications only.
[010] The document US 2008286192 describes a batch process for two-stage pyrolysis of tires. The charcoal material is not ground, but used directly in rubber formulations.
[011] A problem with coal material obtained by pyrolysis of scrap rubber according to prior art methods is the inability to grind the coal material to a particle size that is suitable for use in valuable products. Unacceptably high levels of volatiles that are present in the obtained carbon materials prevent black carbon powder grinding. OBJECTIVES OF THE INVENTION
[012] Therefore, it is an object of the present invention to provide a method of pyrolysis of scrap tires to produce a carbon material that can be ground to produce a black carbon powder that can be used in rubber and thermoplastic compositions.
[013] Another objective of the present invention is to provide a black carbon powder for use as an excipient or reinforcement in rubber having improved properties.
[014] Another objective of the present invention is to provide carbon black powder having the particle size distribution of some commercially available carbon black powders with the use of a much cheaper and more readily available raw material (scrap tires). SUMMARY OF THE INVENTION
[015] The present invention provides, in a first aspect, a method for recycling a scrap rubber, in particular, tires, this method comprises the following steps: i) pyrolysis of a scrap rubber to obtain a coal material; ii) grinding the carbon material obtained in step i) to obtain a black carbon powder;
[016] characterized by pyrolysis, in step i), comprises at least a two-stage pyrolysis process, wherein said two-stage pyrolysis comprises: a) a first pyrolysis stage to obtain an intermediate carbon material and b) a second stage of pyrolysis to obtain a coal material and in which at least one of stages a) or b) is carried out in a rotary kiln.
[017] In one embodiment, in the first stage of pyrolysis a), the percentage of volatiles present in said scrap rubber is reduced to an amount of about 510% by weight based on the total weight of the intermediate carbon material, and in that the intermediate carbon material is introduced into the second pyrolysis stage b), in which the percentage of volatiles is further reduced to a percentage of less than 2.5% by weight, preferably less than 2.0% by weight, based in the total weight of the charcoal material.
[018] In one embodiment, the temperature during the first pyrolysis stage a) is
[019] preferably from 500-800 °C, more preferably 600-700 °C and even more preferably 630-670 °C.
[020] In one embodiment, the temperature during the second stage of pyrolysis b) is
[021] preferably between 550-800 °C, more preferably 650-750 °C and even more preferably 680-720 °C.
[022] In one embodiment, the residence time of each of the first pyrolysis stage a) and the second pyrolysis stage b) is independently between 2050 minutes, preferably 25-45 minutes, and most preferably 30- 40 minutes.
[023] In one embodiment, the residence time of each of the first pyrolysis stage a) and the second pyrolysis stage b) is substantially equal in duration.
[024] In one embodiment, in the second pyrolysis stage a), the percentage volatiles is reduced to less than 1.0% by weight based on the total weight of the carbon material.
[025] In one embodiment, the milling of step ii) is performed by jet milling using compressed air or steam.
[026] In one embodiment, the milling of step ii) is performed so that the black carbon powder obtained from step ii) has a particle size distribution of D50<10 µm and D99<40 µm, preferably a distribution of particle size of D50<5 µm and D99<20 µm, more preferably a particle size distribution of D50<1 µm and D99<10 µm, even more preferably a particle size distribution of D50<0, 5 µm and D99<2 µm.
[027] In one embodiment, an additional pelletizing step ((step iii)) is performed after step ii).
[028] In one embodiment, the pelletizing of step iii) is carried out by mixing a binding agent with the black carbon powder obtained in step ii) and pelletizing the mixture thus obtained to obtain a pelletized black carbon powder.
[029] In one embodiment, the binding agent is pregelatinized starch.
[030] The invention also relates to a black carbon powder derived from scrap rubber, wherein the black carbon powder derived from scrap rubber comprises: a) 60-98% by weight of carbon black, b) less than 2.0% by weight of volatiles, c) 0-30% by weight of silica.
[031] In another embodiment, a black carbon powder derived from scrap rubber, according to the invention, further comprises 1-5% by weight of zinc oxide, based on the total weight of the black carbon powder,
[032] In another embodiment, a carbon black powder derived from scrap rubber, according to the invention, further comprises 1-5% by weight of zinc sulfide, based on the total weight of the carbon black powder.
[033] In another embodiment, the ratio between zinc oxide and zinc sulfide is between 1:10 to 10:1, preferably between 1:2 and 2:1.
[034] In another embodiment, a black carbon powder derived from scrap rubber, according to the invention, has a particle size distribution of preferably D99 less than 30 µm and D50 less than 6 µm, preferably D99 less than 20 µm and D50 less than 4 µm, more preferably D99 less than 9 µm and D50 less than 3 µm, even more preferably D99 less than 4 µm and D50 less than 0.3 µm.
[035] In another embodiment, a carbon powder
[036] Scrap rubber-derived black according to the invention has a BET surface area of at least 60 m2/g, preferably at least 70 m2/g and even more preferably a BET surface area of at least 75 m2/g.
[037] In another embodiment, a black carbon powder derived from scrap rubber, according to the invention, has a particle size distribution of D50<0.5 µm and a BET surface area of at least 75 m2/ g.
[038] In another embodiment, a black carbon powder derived from scrap rubber, according to the invention, has a STSA surface area (of statistical thickness) of between 46-86 m2/g, preferably 59-79 m2/ g, even more preferably 64-74 m2/g.
[039] In another embodiment, a black carbon powder derived from scrap rubber, according to the invention, has a polyaromatic hydrocarbon (PAH) content of less than 0.50 mg/kg, preferably less than 0.25 mg /kg, more preferably less than 0.01 mg/kg.
[040] In another embodiment, a black carbon powder derived from scrap rubber, according to the invention, has an oil absorption number between 67-97 m3/g, preferably 72-92 m3/g, more preferably 77 -87 m3/g.
[041] In another embodiment, a carbon black powder derived from scrap rubber, according to the invention, has a primary particle size of 20-40 nm, preferably 26-36 nm, more preferably 2834 nm.
[042] The invention also relates to a black carbon granule derived from scrap rubber comprising: a) 60-98% by weight of black carbon, b) less than 2.0% by weight of volatiles, c) 0- 30% by weight of silica and d) 0.5 - 1.0% by weight of binding agent.
[043] In yet another embodiment, the black carbon granule derived from scrap rubber, according to the invention, has a binding agent which is starch, preferably pregelatinized starch.
[044] In yet another embodiment, the black carbon powder derived from pelletized scrap rubber, according to the invention, has a starch concentration preferably between 0.1 and 6.0% by weight, more preferably 0.3 and 5.0% by weight, even more preferably 0.5 and 3.0% by weight, even more preferably 0.5 and 1.5% by weight of the total weight of the black carbon granule derived from scrap rubber.
[045] In another aspect of the invention, the invention relates to the use of a black carbon powder derived from scrap rubber, according to the invention, as an excipient or reinforcing agent in a rubber composition, a paint, a paint, a putty, a thermoplastic composition or a thermoplastic elastomer.
[046] In another aspect of the invention, the invention relates to a rubber composition comprising a black carbon powder derived from scrap rubber, according to the invention, said rubber composition having a tensile strength of 15-30 MPa, preferably 20-29 MPa, more preferably 22-28 MPa.
[047] Further embodiments of the present invention are mentioned in the appended claims. The invention will be further elucidated in the detailed description below. DEFINITIONS
[043] The following are definitions of some of the terms used throughout the description and claims.
[044] By 'scrap rubber' is meant rubber waste material. Generally, but not exclusively, this scrap rubber is obtained from tires that are no longer suitable for use.
[045] By ‘coal material’ is meant a solid carbonaceous material obtained from the pyrolysis of a scrap rubber material. Typical components of a carbon material are carbon black, waste material, silica, volatiles and water.
[046] By 'waste material' is meant one or more of an inorganic ash and any other compounds or elements present in the carbon material (or black carbon powder, as defined herein) that constitutes the mass balance of the carbon material . The waste material may optionally contain zinc oxide (ZnO), zinc sulfide (ZnS), titanium dioxide (TiO2), calcium oxide (CaO), aluminum oxide (Al2O3), iron oxide (Fe2O3), oxide magnesium (MgO), sodium phosphorus, bromine, chlorine, potassium and fluorine.
[047] By 'carbon black' is meant a black finely divided form of amorphous carbon. In other words, a virtually pure elementary carbon in the form of colloidal particles. Black carbon is, for example, produced by incomplete combustion or thermal decomposition of gaseous or liquid hydrocarbons under controlled conditions. Its physical appearance is that of a finely divided, black granule or powder. Its use in tires, rubber and plastic products, printing inks and coatings is related to properties of specific surface area, particle size and structure, conductivity and color.
[048] The definition of carbon black, as used herein, does not include soot (finely divided carbon deposited from flames during the incomplete combustion of organic substances such as coal) or black carbon (pure carbon in various bonded forms, obtained through combustion incompleteness of carbon-containing materials). Soot and carbon black are the two most common generic terms applied to many unwanted carbonaceous by-products resulting from the incomplete combustion of carbon-containing materials such as oil, fuels or gasoline, coal, paper, rubber, plastics and waste material. Soot and carbon black also contain large amounts of extractables from dichloromethane and toluene and may have an ash content of 50% or more.
[049] Carbon black is chemically and physically different from soot and carbon black. Most types of black carbon contain more than 97% elemental carbon, said elemental carbon is generally arranged as aciniform particulate (cluster-like cluster).
[050] In the case of commercially available black carbons, organic contaminants such as polycyclic or polyaromatic aromatic hydrocarbons (PAHs; defined below)) are present in extremely small amounts (eg, between 200-736 mg/kg, depending on grade, method manufacturing and type of raw material) and therefore are not considered biologically available.
[051] By 'furnace black carbon' is meant commercially available black carbons derived from the incomplete combustion of liquid hydrocarbons under controlled conditions. This method is suitable for mass production due to its high production and allows wide control of its properties such as particle size or structure. This is currently the most common method used to manufacture carbon black for a variety of rubber reinforcement to color applications. Examples of furnace black carbons include, N110, N220, N330, N550, N660 and N772 manufactured by companies such as Birla Carbon, Cabot Corporation and Orion Engineered Carbons.
[052] By 'thermal black carbon' is meant a black carbon derived from the thermal decomposition of natural gas in the absence of oxygen.
[053] By 'carbon black powder' is meant a powdered form of carbon black. In other words, fine black carbon particulates. Carbon black powder in the composition, according to the invention, obtained by grinding a carbon material, the carbon black powder comprising, for example, carbon black, waste material, silica, volatiles and water.
[054] By ‘black carbon powder derived from scrap rubber’ is meant a black carbon powder derived from a scrap rubber, preferably a black carbon powder that is obtained from the pyrolysis of a scrap rubber.
[055] By 'pyrolysis' is meant a process of thermo-chemical decomposition at elevated temperatures of an organic material in the absence of oxygen.
[056] By 'two-stage pyrolysis' is meant a pyrolysis process that is conducted in at least two separate stages, that is, at least one first stage and at least one second stage. In other words, at least two subsequent pyrolysis processes are carried out. Therefore, it is clear that the invention also relates to two-stage pyrolysis which comprises more than two consecutive steps, for example at least a third pyrolysis step and optionally, for example, at least a fourth pyrolysis step. It is also possible that there are two first stages of pyrolysis, in other words, where an additional stage is introduced between the first and second stages a) and b). The product from the at least first stage pyrolysis is mentioned herein as an intermediate carbon material and the product from the at least second stage pyrolysis is mentioned herein as a carbon material. The at least second pyrolysis stage can also be referred to as the polishing stage. The two stages can be carried out in the same pyrolysis apparatus or in two separate pyrolysis apparatuses. The two stages can be conducted, for example, in a rotary kiln, for example, in two rotary kilns, or, for example, in a batch reactor and a rotary kiln.
[057] By 'rotating oven' is meant a cylindrical vessel, inclined slightly to the horizontal, which is rotated about its axis. The material to be processed is fed to the upper end of the cylinder. As the oven rotates, the material gradually moves downward toward the lower end and can undergo a certain amount of agitation and mixing. Hot gases pass through the greenhouse. Gases can pass through the greenhouse in the same direction as the process material (in current), but preferentially pass through the greenhouse in the opposite direction (countercurrent). Hot gases can be generated in an external furnace, or they can be generated inside the greenhouse, for example, by a flame.
[058] By 'volatile' is meant any element or compound that is removed in a gaseous state during the pyrolysis of scrap rubber. In other words, an element or compound that is readily evaporated. Typically, volatiles released during pyrolysis can be classified as non-condensables and condensables.
[059] 'Non-condensable volatiles' are volatiles having a low boiling point between -200 °C and 80 °C. Examples are hydrogen (H2), methane (CH4, boiling point -162 °C), ethane (C2H6, boiling point -89 °C), propane (C3H8, boiling point -42 °C), butane (C4H10, boiling point 0 °C), pentane (C5H12 , boiling point 36 °C), hexane (C6H14, boiling point 69 °C), carbon monoxide (CO), carbon dioxide (CO2), sulfur (S) or nitrogen (N2). Non-condensable volatiles are present at approximately 10-40% by weight, preferably 15-30% by weight, more preferably 20-25% by weight of the total weight of volatiles. Typically, at least 70% of non-condensable volatiles have a boiling point in the range of -200°C to 80°C.
[060] 'Condensable volatiles' are volatiles having a boiling point between 85 and 290 °C. Condensable volatiles comprise approximately 60-90% by weight, preferably 70-85% by weight, more preferably 7580% by weight of the total weight of volatiles. Condensable volatiles are generally fuel components.
[061] Condensable volatiles have a typical boiling point range between 85 °C and 138 °C, between 139 °C and 155 °C, between 156 °C and 180 °C, between 181 °C, and 206 °C , between 207 °C and 245 °C, between 246 °C and 270 °C or between 271 °C and 290 °C. Typically, at least 70% of the condensable volatile components have a boiling point in the range of 85°C and 290°C.
[062] By 'dwell time' is meant the length of time or duration in which the material is present in the pyrolysis apparatus, during the pyrolysis step itself. In other words, the time during which the pyrolysis process takes place. In other words, the time during which the pyrolysis apparatus is in operation. In other words, the reaction time of the pyrolysis process.
[063] By 'grinding' is meant the process of breaking a material (in the present invention, the coal material) into smaller particles, preferably individual particles (ie, non-agglomerated) or small agglomerates (eg, smaller than 40 microns in diameter). The material which is obtained after milling is, in the present invention, a black carbon powder. The person skilled in the art is familiar with various methods suitable for grinding coal material. Examples of such milling methods and apparatus are fluidized bed opposite jet mills and spiral jet mills in combination with air classifiers.
[064] With "D99 particle size distribution" or "D50 particle size distribution" is meant the 99th and 50th percentage of the particle size distribution, respectively, as measured by volume. D99 describes a sample of particles, with which 99% by volume of the particles have a size smaller than the stated particle size distribution. With D99 < x micrometer it is understood that 99% by volume of the particles have a size of less than x micrometer. The D50 describes a sample of particles, with which 50% by volume of the particles have a size smaller than the stated particle size distribution. With D50 < x micrometer it is understood that 50% by volume of the particles have a size of less than x micrometer.
[065] Black carbon particle size distribution is an important property. For a given carbon black loading, black intensity and booster power increase with decreasing particle size distribution.
[066] The shape and size of aggregates (structure) also affect an end use performance of carbon black, as the larger carbon black structure increases viscosity and improves dispersion. The rigidity (modulus) of elastomeric systems becomes significantly greater with increasing structure. The preferred method for measuring these properties is transmission electron microscopy.
[067] Particle size distribution can be determined according to the method disclosed in: ASTM D3849 - 2011. Particle size distribution can also be determined using wet or dry laser diffraction in an instrument such as a Malvern Mastersizer S See 2.19. If a wetting agent is required, it can be, for example, a mixture of the commercially available products Morvet® + Supragil® (ratio 70:30). A person skilled in the art will know which type of wetting agent is suitable for use during a wet laser diffraction measurement. External ultrasound can be applied to prevent particle aggregation. More details on the exact conditions used for measurements in the present invention can be found in the examples below.
[068] With 'BET surface area' is meant the surface area and porosity of the particles present in a sample. BET surface area is a measure of the physical adsorption of gas molecules on a solid surface and serves as a basis for an important analysis technique for measuring the specific surface area of carbon black. BET measures the specific surface area of 1 gram of carbon black, expressed in square meters. The BET surface area, therefore, provides information about the physical adsorption of molecules and gas onto a solid surface. Molecules of an adsorbate gas are physically adsorbed onto particle surfaces, including the inner surfaces of any pores, under controlled conditions within a vacuum chamber. An adsorption isotherm is obtained by measuring the gas pressure above the sample as a function of the volume of gas introduced into the chamber. The linear region of the adsorption isotherms can then be used to determine the volume of gas needed to form a monolayer across the available particle surface area, using BET theory, as described by the following equation:

[069] where v is the volume of gas, P is the pressure, Po is the saturation pressure, vm is the volume of gas needed to form a monolayer and c is the constant BET. The trace of relative pressure, Φ (=P/P0), and volume allows the volume of a monolayer to be determined from the gradient and crossing of the line. The specific surface area can then be calculated using the cross-sectional area of the gas molecules, the molecular volume of the gas and the weight of the sample. BET surface areas can be measured in accordance with ASTM D-6556-2010.
[070] With 'statistical thickness surface area' or 'STSA' is meant the specific surface area that is accessible to rubber, per square meter per gram (m2/g). This is used by the rubber industry to define the fineness level of carbon black - the higher the number, the lower the carbon black. This can be measured according to ASTM D-6556-2010.
[071] 74 By ‘polyaromatic hydrocarbon’ or polycyclic aromatic hydrocarbon’ or ‘PAH’ is meant a class of molecules consisting of aromatic, fused carbon rings that do not contain heteroatoms or carry substituents (other than hydrogen). Examples of PAHs include, but are not limited to, Benzo(a)anthracene, (CAS 56-553) Benzo(a)phenanthrene (chrysene), (CAS 218-01-9), Benzo(a)pyrene, (CAS 50-32- 8), Benzo(b)fluoranthene, (CAS 205-99-2) Benzo(j)fluoranthene (CAS 205-82-3), Benzo(k)fluoranthene, (CAS 207-08-9), Benzo(j, k)fluorene (fluoranthene), (CAS 206-44-0), Benzo(r,s,t)pentaphen, (CAS 189-55-9) Dibenz(a,h)acridine (CAS 226-36-8), Dibenz(a,j)acridine (CAS 224-42-0), Dibenzo(a,h)anthracene (CAS 53-70-3) Dibenzo(a,e)fluoranthene (CAS 5385-75-1), Dibenzo(a ,e)pyrene (CAS 192-65-4), Dibenzo(a,h)pyrene (CAS 189-64-0), Dibenzo(a,l)pyrene (CAS 191-30-0), 7H-Dibenzo(c ,g)carbazole (CAS 194-59-2), 7,12Dimethylbenz(a)anthracene (CAS 57-97-6), Indene(1,2,3cd)pyrene (CAS 193-39-5), 3-Methylcholanthrene (CAS 56-49-5), 5-Methylchrysene (CAS 3697-24). Nitropyrene (CAS 5522-43-0), Acenaphthene, (CAS 83-32-9), Acenaphthylene (CAS 208-968), Anthracene (CAS 120-12-7), Benzo(g,h,i)perylene (CAS 19124-2), Fluorene (CAS 86-73-7), Phenanthrene (CAS 85-01-8), Pyrene, (CAS 129-00-0).
[072] By 'primary particle size' is meant the size of a particle of carbon black powder as measured by diffraction methods. Primary particle size can be measured in accordance with ASTM D6556-2010. Black carbons do not exist as primary particles as such. During the manufacture of black carbon, the primary particles fuse together to form aggregates. The shape and degree of branching of the aggregate is referred to as structure. Increasing the structure typically increases the compound's modulus, hardness, electrical conductivity and viscosity and improves carbon black's dispersibility. Typical carbon black primary particle size ranges from 8 nanometers for furnace blacks to 300 nanometers for thermal blacks. Finer particles (namely, having a primary particle size of less than 50 nanometers) increase reinforcement, abrasion resistance, and improve tensile strength.
[073] [075] With ‘oil absorption number’ or ‘OAN’ is meant the number of grams of oil required to bind one gram of particles. Oil absorption is the measure of structure with a high number representing larger structure. Oil absorption is measured in accordance with ASTM D-2414-2012. Generally speaking, high frame blacks impart greater levels of mechanical reinforcement to a rubber compound (eg tensile strength) and lower dynamic performance (eg bounce resilience as defined below), while low frame blacks impart relatively lower levels of mechanical reinforcement and better dynamic performance.
[074] With 'stress strength' is meant the stress that a particle can withstand without deformation, as measured in force per unit area, N/m2 or MPa. Tests were conducted in accordance with ISO 37-2011.
[075] By 'cross density' is meant the difference between the maximum and minimum torque as measured in a rubber compound using an Oscillating Disk Rheometer (ODR) or a Motion Matrix Rheometer (MDR), commonly referred to as value of “MHML” or “Delta S”.
[076] By 'binding agent' is meant a substance that allows the agglomeration of individual particles of carbon black powder into fluidizing granules of adequate structural strength and improves stability. A binding agent is also known in the art as a binder.
[077] With ‘SBR’ is meant styrene-butadiene rubber. SBR describes a family of synthetic rubbers derived from styrene and butadiene. These materials have good abrasion resistance and good aging stability when protected by additives. SBR is the most common rubber from which tires are made. The styrene/butadiene ratio influences the polymer properties: with high styrene content, rubbers are harder and less flexible.
[078] By ‘EPDM’ is meant ethylene-propylene-diene monomer rubber (class M). Class M refers to its classification in ASTM standard D-1418-2010. Class M includes rubbers having a saturated chain of the polymethylene type. Dienes currently used in the manufacture of EPDM rubbers are dicyclopentadiene (DCPD), ethylidene norbornene (ENB), and vinyl norbornene (VNB).
[079] With ‘DeMatia flex fatigue’ is meant the resistance of a rubber compound to cyclic bending and is measured in accordance with ISO 132-2011.
[080] With ‘M100’ is meant the tension measured at 100% force on a standard bell-shaped rubber. M100 is measured in accordance with ISO 37-2005.
[081] With ‘M300’ is meant the strain measured at 300% force on a standard bell-shaped rubber. M300 is measured according to ISO 37-2005.
[082] By 'stretching' is meant the final stretch in breaking a standard bell-shaped rubber. Elongation is measured in accordance with ISO 37-2005.
[083] With 'bounce resilience (Schob)' is understood the percentage of resilience of a rubber compound as an indication of hysteretic energy loss which can also be defined by the relationship between storage modulus and loss modulus. The percentage of rebound measured is inversely proportional to the hysteretic loss. Bounce resilience is measured in accordance with ISO 4662-2009.
[084] With ‘PHR’ is meant Parts for Hundreds of Rubber. PHR is a measure that is used by rubber chemists to portray how much of certain ingredients is needed in a rubber makeup. DETAILED DESCRIPTION
[085] The inventors have discovered a method for recycling a scrap rubber, in particular, tires, this method comprises the following steps: i) pyrolysis of a scrap rubber to obtain a coal material; ii) grinding the carbon material obtained in step i) to obtain a black carbon powder;
[086] characterized by pyrolysis, in step i), comprises at least one two-stage pyrolysis process, wherein said two-stage pyrolysis comprises:
[087] a first pyrolysis stage to obtain an intermediate carbon material and
[088] a second pyrolysis stage to obtain a coal material and in which at least one of stages a) or b) is carried out in a rotary kiln.
[089] The invention is based on the following. First, the inventors found that the particle size of the black carbon derived from prior art scrap rubber is too large to meet today's demands for carbon black powders. The inventors have further found that grinding the charcoal material obtained from the prior art scrap rubber pyrolysis processes is not sufficiently possible. Later, the inventors inventively discovered that this problem with grinding was, at least partially, due to the high volatile content of the coal material. Subsequently, the inventors invented the present two-stage pyrolysis process in order to provide coal material having a lower volatile content. This inventive carbon material is suitable for grinding to a smaller particle size and thus meets current needs in the black carbon field.
[090] In other words, the inventors invented a new process for recycling scrap rubber, preferably tires. The present method of recycling comprises the steps of i) pyrolysis of the scrap rubber to obtain a carbon material and ii) grinding the carbon material thus obtained to obtain a black carbon powder, wherein the pyrolysis step consists of at least two stages.
[091] The scrap rubber (preferably scrap tires) that can be used in the method, according to the invention, can be any type of rubber, preferably vehicle tires. Although there is a discussion below of the present method in relation to tires, it should be noted that the present invention is not limited to tires. Scrap tires are processed in the form of particles, for example in the form of granules or chips. Preferably, the scrap rubber particles (used as the scrap rubber in the present invention) have a maximum particle size of 30 x 30 x 30 mm, more preferably a maximum particle size of 20 x 20 x 20 mm, further more preferably a maximum particle size of 10 x 10 x 10 mm.
[092] The rubber composition used in a vehicle tire is specific to the tire's function. In other words, when manufacturing a tire, its composition is selected for the type and function of the tire being produced. For example, truck tires are typically low in silica (approximately 5% by weight, based on the total weight of the rubber composition). Car tyres, specifically passenger car tyres, can be designated as 'low silica' (approx. 10% by weight, based on the total weight of the rubber composition) or 'high silica' (approx. 15% by weight , based on the total weight of the rubber composition). The addition of silica to a rubber is believed to result in a reduction in rolling resistance. Rolling resistance is defined as the amount of energy a tire absorbs as it rotates and deflects. Assuming correct tire pressures are maintained and assuming varying speed and different drive characteristics, a 20% reduction in rolling resistance can be achieved by adding silica to the rubber composition used for automobile tires. The lower the rolling resistance, the less fuel is needed to propel the vehicle forward. The reduction in rolling resistance, however, commonly results in a reduction in wet grip performance, which is, in fact, unacceptable. For this, a compromise is sought during the manufacture of a tire between reducing rolling resistance, on the one hand, and increasing wet grip performance, on the other hand. Depending on the type and function of the tires, the optimal amount of silica is selected.
[093] Given the variety of scrap tires, the method according to the invention is suitable for pyrolysis of scrap rubber with varying amounts of silica. Preferably, the raw material tires used to prepare the scrap rubber used as a starting material in the present method have a silica content of less than 15%, more preferably less than 10% and even more preferably less than 5%.
[094] The raw material tires (used to prepare the scrap rubber used as a starting material in the present method) are, in one embodiment of the present invention, reduced in size and fed to the pyrolysis apparatus by means of a tightening of gravimetric feeding. The pyrolysis apparatus can be, for example, a rotary oven that operates in a two-stage mode. Briefly, the rotary kiln is a rotating cylinder inclined at an angle (for example, an angle of 1.5°) that is enclosed in a furnace along its active length and can be equipped with hermetic gas seals that prevent exchange between the internal atmosphere and the local ambient conditions. As the cylinder rotates, material is gently spilled as it flows from the feed end of the cylinder to the discharge end.
[095] For example, pyrolysis can be performed in an indirectly heated rotary oven that is preferably gas heated or electrically heated. Preferably, at least one or both of stages a) and b) of the pyrolysis are carried out in a rotary oven operating in countercurrent flow. The rotary kiln can be prepared for continuous pyrolysis of the scrap rubber raw material which operates in countercurrent flow. By countercurrent flow, it is understood that the oils (namely, the condensable volatiles) and vapors (namely, non-condensable volatiles) released during the pyrolysis step are removed from the rotary kiln on the meso side of the kiln in which the material- raw (scrap rubber) is added. Typical technical parameters for this rotary kiln are an overall span of 9.0 m, an internal diameter of 0.4 m, a heating zone span of 3.0 m in a nitrogen atmosphere (oxygen free atmosphere) with a rotational speed of 1 - 2 RPM, eg 2-3 RPM, eg 3-4 RPM, eg 4-5 RPM.
[096] The construction and operation of this rotary kiln, as discovered by the inventors, allows a two-stage pyrolysis to be performed, in which the scrap rubber is heated to a first temperature during stage a) and then to a second temperature during stage b), which is preferably higher than the first temperature. The resulting charcoal material obtained after the second pyrolysis stage b) has a low volatile content, preferably less than 2.0% by weight and the charcoal material thus obtained can then be ground to obtain a black carbon powder. .
[097] The invention, however, is not limited to the use of only a rotary stove. For example, a first pyrolysis stage a) can take place in a first rotary kiln and the second pyrolysis stage b) in a second rotary kiln. In this configuration, the second kiln is referred to as a polishing kiln and, by using this polishing kiln, a very low volatile content can be achieved.
[098] In a further example, the first pyrolysis stage a) can be conducted in a batch reactor which is known PER SE in the art. The second pyrolysis stage b) can then be carried out in a rotary oven. A batch reactor has a disadvantage over an oven operating in continuous mode in that a batch reactor can contain only a limited amount of raw material and must be alternately filled, the pyrolysis step conducted and then emptied. However, obtaining an intermediate coal material from a batch reactor and then subjecting the thus obtained intermediate coal material to a second stage of pyrolysis in a rotary kiln operating in accordance with the invention would allow an inventive coal material be produced with a low volatile content.
[099] Without wishing to be bound by any theory, the present inventors have discovered that if the coal material comprises more than 5% by weight of volatiles, the milling of the obtained coal material is difficult and leads to a low-grade product which it does not have the necessary dispersion, particle size distribution or reinforcing qualities needed to be used in rubber or thermoplastic compositions.
[100] The pyrolysis of scrap rubber from
[101] according to the invention, allows the carbon material to be ground, so that a black carbon powder is obtained that can be used in valuable end products. One or more of the aims of the invention are therefore achieved.
[102] In one embodiment of the invention, in the first pyrolysis stage a), the percentage of volatiles in the scrap rubber is reduced to an amount of about 5-10% by weight based on the total weight of the intermediate carbon material.
[103] In another embodiment of the invention, in the second stage of pyrolysis b), the percentage of volatiles present in said intermediate carbon material is reduced to a percentage of less than 2.5% by weight based on the total weight of the carbon material. coal.
[104] The two-stage process according to the present invention allows the percentage by weight of volatile compounds to be reduced to less than 10% by weight after the first stage, and to less than 2.5% by weight, preferably less than 2.0% by weight after the second stage. This low volatile content of the final product cannot be obtained by the methods present in the prior art. The inventors found that volatiles are preferentially removed in a rotating oven. Without wishing to be bound by any theory, a rotating oven allows volatiles to be more easily removed from the pyrolysis process. Specifically, a pyrolysis process comprising a first and a second pyrolysis stage is sufficiently efficient to reduce the volatile content to below the desired 2.0% by weight level in an economically viable manner. This contrasts with the typical batch process, in which the coal material obtained from it has a volatile content ranging from about 6% to 15%. However, a batch process is quite suitable for use during at least one first stage of pyrolysis.
[105] Preferably, a flow against
[106] gas stream is applied to the rotary kiln during its operation. A countercurrent flow allows a coal material to be produced with a low percentage by weight of volatile compounds. This is because gases are removed from the product and thus any volatiles, which become free during the pyrolysis step, do not remain in contact with the charcoal material and thus cannot be reabsorbed by the charcoal material. In other words, the use of a countercurrent flow during pyrolysis increases the volatile reduction production.
[107] In one realization, the temperature
[108] during the first pyrolysis stage of the pyrolysis in step i) is preferably 500-800 °C, more preferably 600-700 °C and even more preferably 630-670 °C. The advantages of these variations are that the condensable volatiles and the more readily removed fractions of the volatile components (namely the non-condensable volatiles) can be removed without leading to increased (or advanced) decomposition of the intermediate carbon material.
[109] In one realization, the temperature
[110] during the second pyrolysis stage of the pyrolysis step in i) is preferably between 550-800 °C, more preferably 650-750 °C and even more preferably 680-720 °C. The advantage of these variations is that the less volatile fraction of the volatile components in the intermediate carbon material is removed without causing further unwanted decomposition of the carbon material. If the temperature is too high, physical and chemical reactions can take place in the carbon material. For example, the structure of carbon black can be adversely affected and the carbon can be oxidized by any residual oxygen species present in the pyrolysis apparatus.
[111] The temperature of the first and/or second
[112] pyrolysis stage is hereby understood to mean the temperature to which the pyrolysis apparatus is heated. The temperature during the first and/or second pyrolysis stages is preferably substantially constant during the residence time. By substantially constant is meant a deviation of at most ± 10% from the set temperature (namely the temperature at which the pyrolysis apparatus is set) during the residence time.
[113] For example, a rotating greenhouse can be divided into zones and each zone heated independently. For example, in a rotary greenhouse subdivided into four zones, zone 1 and zone 2 can be heated to 630 °C and zone 3 and zone 4 can be heated to 680 °C. Therefore, it is clear that zones 1 and 2 comprise the first pyrolysis stage and zones 2 and 3 comprise the second pyrolysis stage. In fact, there are additional possible combinations of zones and temperatures that are within the scope of the invention.
[114] Preferably, the temperature in the second pyrolysis stage a) is higher than in the first pyrolysis stage b), as this higher temperature collects the less volatile components of the carbon material.
[115] More preferably, the temperature in the second pyrolysis stage a) is at least 30 °C, preferably at least 50°C higher, more preferably at least 80 °C higher, than in the at least first pyrolysis stage b) , as this higher temperature collects the less volatile components of the coal material. In this way, the first stage of pyrolysis removes the first part of all volatiles at a lower temperature to reduce any risk of decomposition. During the second pyrolysis stage, a large part of the remaining volatiles is removed, which cannot be removed as easily at the lower temperature at which the first pyrolysis stage is carried out (at least not acceptable during dwell times). This is because, during the second stage of pyrolysis, the temperature is increased.
[116] In one embodiment, the residence times of each of the first pyrolysis stage a) and the second pyrolysis stage b) are independently between 20-50 minutes, preferably 25-45 minutes, and most preferably 30-40 minutes.
[117] In one embodiment, the residence time of each of the first pyrolysis stage a) and the second pyrolysis stage b) is substantially equal in duration. Substantially equal means a deviation of at most ± 10% of the residence time between the first and second pyrolysis stages. For example, if the residence time of the first pyrolysis stage is 35 minutes, then the residence time of the second pyrolysis stage must be between 32.5 and 38.5 minutes in order to be marked as having a residence time. substantially equal.
[118] In another embodiment, the residence time of the first stage of pyrolysis is as mentioned above (namely, between 20-50 minutes, preferably 25-45 minutes and more preferably 3040 minutes) and the residence time of the second stage of pyrolysis b) is shorter, preferably the residence time of the second pyrolysis stage is between 5-10 minutes, more preferably 10-15 minutes and even more preferably 15-20 minutes.
[119] The advantage of this realization (in other words, one realization of the residence time of the first pyrolysis stage is substantially greater than the residence time of the second stage of pyrolysis) is that the raw material material is not in contact with the increased heat of the kiln, as used during the second stage of pyrolysis, for an extended period of time, thus preventing unwanted decomposition of the charcoal material. Furthermore, an optimal on-call time ensures that the process takes place at an economical rate.
[120] The inventors discovered after experiment that there are preferred temperatures and residence times in order to optimize the volatile content of the coal material. The temperature of the first stage is chosen to reduce the volatile content of the charcoal material to less than 10% by weight, and the temperature of the second stage is chosen to reduce the content of the charcoal material to less than 2.5% by weight, more preferably less than 2.0% by weight. Importantly, the use of the two-stage temperature profile described above, for example, in a rotary kiln operating in counter-current mode, is that the total process time is vastly reduced compared to the batch process for rubber pyrolysis of scrap.
[121] In an example of the invention, the full-step pyrolysis lasts between 30 minutes and 80 minutes. This is considerably less than comparable methods in the prior art, where the step pyrolysis lasts on the order of several hours instead of minutes. Subsequently, the invention provides a more economical means for pyrolysis of scrap rubber. There is an energy benefit to the two-step pyrolysis invention compared to the batch process, associated with a reduction in residual energy due to volatile resorption. The invention removes volatiles much more efficiently than the prior art completely batch process, due to the continuous flow of gas flowing through a rotary kiln (used in at least one of the pyrolysis stages). volatile is therefore reduced and thereby also facilitates the possibility of reducing the final volatile content to below 2.0% by weight in an economically viable manner.
[122] In one embodiment, in the second stage of pyrolysis in step i) the percentage of volatiles is reduced to a percentage of less than 1.0% by weight, where the % by weight is based on the total weight of the carbon material after step i).
[123] The advantage of a volatile content of less than 1.0% by weight is that this carbon material can be ground into finely divided carbon black powder. The resulting ground black carbon powder has a particle size of less than 50 nm, so it can be incorporated into valuable end products. Pyrolysis, according to the invention, allows this low percentage of volatiles to be reached.
[124] In one embodiment, step ii) is performed by jet milling using compressed air or steam.
[125] Carbonaceous coal material provided by the two-stage pyrolysis process, after step i), can be reduced to finely divided particles or “down” form by known spraying techniques. However, mixing and dispersing finely divided particles of carbonaceous carbon material into rubber and plastics is known to be problematic. Therefore, a milling step ii) is conducted to prepare a carbon black powder with a defined particle size distribution.
[126] The advantage of the charcoal material according to the invention over the prior art charcoal material is that the charcoal material according to the invention does not block or obstruct the grinding apparatus. This is due to the low volatile content of the carbon material according to the invention.
[127] The grinding step can be conducted in a vibrating mill, a jet mill (air) or a combination of a vibrating mill and a jet mill (air). The inventors found that a combination of a vibrating mill and an air jet mill gives a particle size distribution of D50 < 2.3 µm and D99 < 9.2 µm, which produces a black carbon powder suitable for use. on high quality products. However, for certain uses, grinding using a vibrating mill, producing a particle size distribution of D50 <9.0 µm and D99 < 35.0 µm, could be sufficient. For example, grinding can be conducted in a laboratory-sized mill at a temperature of 20 °C and a classifier speed of 22,000 rpm, using air as a medium, at a pressure of 3 bar. Hot air up to around 220 °C or superheated steam at a temperature of around 300 °C can also be used. Classifier air velocities, in terms of RPM, will vary with the diameter of the classifier well, because the peripheral velocity of the well will increase for a given RPM as the diameter increases. For example, a laboratory jet mill can operate at 22,000 RPM, while an industrial-scale machine, having a diameter of 800 mm, can achieve the same results at a speed of around 6000 RPM.
[128] In one embodiment, step ii) is performed so that the black carbon powder obtained from step ii) has a particle size distribution of D50<10 µm and D99<40 µm, preferably D50<5 µm and D99<20 µm, more preferably D50<1 µm and D99<10 µm, even more preferably D50<0.5 µm and D99<2 µm.
[129] The advantage of grinding a coal material according to the invention is that a particle size distribution of D50<10 µm and D99<40 µm can be obtained. In other words, less than 50% of particles have a particle size of 10 µm and less than 99% of particles have a particle size of 40 µm. In one embodiment, step ii) has a particle size distribution of D50 < 1 µm and D99 < 4 µm. In other words, less than 50% of the particles have a particle size of 1.0 µm and less than 99% of the particles have a particle size of 4.0 µm.
[130] There are several grades of black carbon on the market. An example of this grade is N550, having a D50 <2.1 µm and a D99 < 6.2 µm. Another example of this grade is N650 having a D50 < 2.6 µm and D99 < 10.9 µm. For these grades, the combination of a certain upper limit for D50 and a certain upper limit for D99 is necessary to provide a level of quality control between batches. However, other characteristics of these black carbons.
[131] In one embodiment, an additional pelletizing step ((step iii)) is performed after step ii). In other words, the present method comprises a two-stage pyrolysis step, a milling step and a pelletizing step in the present aspect of the invention.
[132] In order to improve the handling and storage of black carbon powder obtained by grinding, an additional processing step can be done. Black carbon powder can be pelletized. A loose powder could provide some difficulties during storage and handling compared to a pelleted product. A variety of methods for converting individual carbon black particles into granules for improved mixing and dispersion are known in the art. For example, a finely divided carbon black can be agitated under dry conditions in order to reduce the amount of air or other gases associated with carbon black and cause a degree of agglomeration of particles other than carbon black.
[133] In one embodiment, step iii) is carried out by mixing a binding agent with the black carbon powder obtained in step ii) and pelletizing the mixture thus obtained to obtain a pelletized black carbon powder.
[134] The use of a binding agent is known in the art as pelletizing under wet conditions. Under these conditions, the finely divided carbon black can be stirred in the presence of sufficient liquid pelletizing medium, such as water, or a dilute aqueous solution of a binding agent. Suitable binding agents include, among others, sugar, molasses, dextrin, starch, calcium lignin sulfonate and the like. The binding agents allow the agglomeration of individual particles into free-flowing granules of adequate structural potency and enhance stability. A suitable pelletizing agent is, for example, starch, preferably pregelatinized starch. Starch can be added at up to 0.5% by weight, preferably up to 1.0% by weight, based on the total weight of the carbon black powder. Pelleted carbon black powder is therefore easy to handle and is easier to store than powdered carbon black.
[135] In one embodiment of the present invention, a cooling step (step iv) is performed between the pyrolysis step and the milling step. During this cooling step, the charcoal material obtained during the pyrolysis step is cooled before being introduced to the grinding step.
[136] In one embodiment of the present invention, a ferromagnetic metal removal step (step v) is performed prior to the milling step. In some tyres, in particular, truck tire steel (ferromagnetic metal) may be present as reinforcement, this metal could have a detrimental effect on the grinding process. The use of magnets or magnetic separation is preferable for this step. A technician in the subject will know which equipment to use for this step.
[137] The invention also relates to a black carbon powder derived from scrap rubber, wherein the black carbon powder derived from scrap rubber comprises: a) 60-98% by weight of carbon black, b) less than 2.0% by weight of volatiles, c) 0-30% by weight of silica.
[138] The composition of carbon black powder according to the invention is surprisingly low in volatiles. This low volatile content is due to the inventive two-stage pyrolysis method. The composition of carbon black powder is different depending on the composition of the raw material. For example, when truck tires are used, a typical carbon black powder composition comprises 88% by weight carbon black, 2.7% by weight silica, 6.5% by weight waste material, 2.3 % by weight of volatiles and 0.5% by weight of water. For example, when the raw material is low silica automobile tires, a typical carbon black powder composition comprises 75% by weight carbon black, 13.9% by weight silica, 7.8% by weight material of residue, 2.2% by weight of volatiles and 0.5% by weight of water. For example when the raw material is high silica automobile tires, a typical carbon black powder composition comprises 66% by weight carbon black, 23.6% by weight silica, 8.0% by weight carbon black material. residue, 1.9% by weight of volatiles and 0.5% by weight of water.
[139] In another embodiment, the carbon black powder has an amount of zinc oxide between 1-5% by weight, based on the total weight of the carbon black powder.
[140] In another embodiment, the carbon black powder has an amount of zinc sulfide between 1-5 % by weight, based on the total weight of the carbon black powder.
[141] Zinc oxide and zinc sulfide are important reagents in activating curing sulfur in the rubber composition, which is a part of the tire manufacturing process. The inventors have discovered that it is possible to substantially reduce the amount of zinc oxide that is required to be added to rubber formulas (cured with sulfur) when the present black carbon scrap rubber powder is used as an excipient, compared to when the prior art black carbon is used. This is due to the presence of zinc oxide and zinc sulfide in the black carbon powder derived from scrap rubber. For example, at least 3 parts percent rubber (PHR). Zinc oxide must be added to prior art furnace black carbon in order to obtain maximum cross density in an ASTM D3191-2010 SBR Test Compound, compared to only 1.5 (PHR) when carbon black powder Scrap rubber derivative, according to the invention, is used.
[142] Any reduction in the use of ZnO will benefit the environment by reducing consumption of the finite and rapidly declining natural resource of zinc-a, which is a cause for global concern. Zinc oxide has also been identified as being an environmentally harmful substance, so any reduction in its use is beneficial.
[143] In another embodiment, the present carbon black powder derived from scrap rubber has a particle size distribution of D50<10 µm and a BET surface area of at least 66 m2/g. In other words, at least 50% of the particles of carbon black powder according to the invention have a particle size distribution of less than < 10 µm and the particles have a BET surface area (as defined above) of at least 66 m 2 /g. High surface area is associated with high polymer:excipient interaction and therefore high reinforcement levels, defined by increased rubber reinforcement levels. A D99 particle size distribution of less than 10 µm is required to incorporate carbon black powder into valuable end products. For other less valuable end products, a higher D99 value may suffice.
[144] In another embodiment, a black carbon powder derived from scrap rubber has a particle size distribution of preferably D99 less than 30 µm and D50 less than 6 µm, preferably D99 less than 20 µm and D50 less than 4 µm , more preferably D99 less than 9 µm and D50 less than 3 µm, even more preferably D99 less than 4 µm and D50 less than 0.3 µm.
[145] In another embodiment, black carbon powder derived from scrap rubber, according to [SIC], has a particle size distribution of D50<0.15 µm and D99<0.5 µm. In other words, carbon black powder according to the invention has the same particle size distribution as furnace black products N550 and N660, which is surprising in view of the prior art black carbon derived of scrap rubber, which has a particle size distribution of at least 100 µm.
[146] In another embodiment, a black carbon scrap rubber powder according to the invention has a STSA surface area (statistical thickness) between 46-86 m2/g, preferably 59-79 m2/g, even more preferably 6474 m 2 /g. STSA provides an indication of the reinforcing properties of carbon black when compounded in a rubber compound. An STSA of between 46-86 m2/g, preferably 59-79 m2/g, even more preferably 64-74 m2/g is desirable in order to obtain sufficient reinforcement characteristics.
[147] In one embodiment, a black carbon powder derived from scrap rubber, according to the invention, has a polyaromatic hydrocarbon (PAH) content of less than 0.50 mg/kg, preferably less than 0.25 mg /kg, more preferably less than 0.01 mg/kg. Two-stage pyrolysis according to the invention also provides a means to control the polyaromatic hydrocarbon content in carbon black powder. PAH is also exceptionally low compared to other black carbons derived from scrap rubber. For example less than 0.5 mg/kg, preferably less than 0.25 mg/kg, more preferably less than 0.01 mg/kg. This low PAH content cannot be achieved in a one-step pyrolysis process. Typically, after a one-step pyrolysis process, carbon black has a PAH content of 71 mg/kg, even if the volatile content is only 2.9% by weight.
[148] The invention therefore provides a surprising level of control over the PAH content of carbon black powder in accordance with the invention. Controlling the level of PAH is highly important as PAHs are carcinogens and as such are controlled substances whose levels should be kept as low as possible in accordance with industry guidelines.
[149] In another embodiment, a black carbon powder derived from scrap rubber, according to the invention, has an oil absorption number between 67-97 m3/g, preferably 72-92 m3/g, more preferably 77 -87 m3/g. The advantage of having an oil absorption number between 67 and 87 m3/g is that higher mechanical strengthening properties, such as tensile strength, can be obtained.
[150] In another embodiment, the carbon black powder derived from scrap rubber of the invention has a primary particle size of 20-40 nm, preferably 26-36 nm, more preferably 28-34 nm. The carbon black powder according to the invention has a highly defined primary particle size of 2040 nm, preferably 26-36 nm, more preferably 28-34 nm. The invention therefore provides a means to control particle size. This is important since the carbon black particle size dimension determines the strength and reinforcing characteristics of the rubber composition in which carbon black powder is used. In addition, carbon black powder according to the invention has a primary particle size in the same order of magnitude as commercially available furnace derived carbon black, for example the N500 series has a typical primary particle size between 40 nm and 48 nm and the N600 series has a typical primary particle size between 49 nm and 60 nm.
[151] Without wishing to be bound by any theory, the milling step provides a means of de-agglomeration of large “heaped” particles of coal material into finer particles. The finer the particles are ground, the more the primary particles are exposed. Therefore, the BET surface area can be controlled by controlling the D99 particle size distribution during the milling process.
[152] The invention also relates to a black carbon granule derived from scrap rubber comprising: a) 60-98% by weight of black carbon, b) less than 2.0% by weight of volatiles, c) 0- 30% by weight of silica and d) 0.5 - 1.0% by weight of starch.
[153] All of the realizations mentioned for the black carbon powder derived from scrap rubber are also applicable for the black carbon granule derived from scrap rubber.
[154] In another embodiment, the black carbon granule derived from scrap rubber has a binding agent which is pregelatinized starch.
[155] In another embodiment, the black carbon granule derived from scrap rubber has a starch concentration, preferably pregelatinized starch preferably between 0.1 and 6.0% by weight, more preferably 0.3 and 5.0% by weight, even more preferably 0.5 and 3.0% by weight, even more preferably 0.5 and 1.5% by weight of the total weight of the black carbon granule derived from scrap rubber. The weight percentage of the binding agent is optimized to produce a granule suitable for blending into rubber compositions. If the weight percentage is too low, the bead will not stick together, and if the binding agent weight percentage is too high, the bead will not disperse in the rubber compounding step.
[156] The invention also relates to the use of a black carbon powder derived from scrap rubber, in accordance with the present invention, or obtained by the present methods in one or more of a rubber composition, a paint, a paint, a bitumen, a thermoplastic composition and a thermoplastic elastomer. The inventive black carbon powder or granule can be incorporated as a reinforcing additive, for example in SBR and EPDM rubbers.
[157] The invention also relates to a rubber composition comprising a black carbon powder derived from scrap rubber, according to the invention, having a tensile strength of 15-30 MPa, preferably 2029 MPa, more preferably 22- 28 MPa. When carbon black powder according to the invention is used in an EPDM rubber as a reinforcing component, the EPDM rubber has a tensile strength of more than 15 MPa. For example, an EPDM rubber comprising 100 PHR of black carbon powder, according to the invention, has a tensile strength of 15.7 MPa, compared to 15.5 MPa or 15.9 MPa when N600 and N500 are used respectively. . Black carbon powder derived from scrap rubber, therefore, imparts advantageous properties to EPDM rubber. This is surprising in view of other black carbons derived from scrap rubber produced by prior art methods.
[158] Also, in an SBR rubber composition, for example, the black carbon derived from scrap rubber according to the invention also has a positive effect on the mechanical properties of the rubber. When 50 PHR units of carbon black powder according to the invention are added to the SBR composition, the resulting composition has a tensile strength of 25.1 MPa. This remarkably high tensile strength is comparable to the tensile strength obtained in a SBR composition comprising commercially available furnace black N550 (25.2 MPa) and even better than the tensile strength of a SBR composition comprising commercially available furnace black N600 available (21.6 MPa). Other standard means of measuring the mechanical properties of a rubber composition, for example the DeMattia flex fatigue test and bounce resilience (Schob) are also comparable between carbon black carbon powder comprising the rubber composition and black furnace comprising rubber composition.
[159] The mechanical properties of rubber compositions comprising black carbon powder derived from scrap rubber, according to the present invention, are similar, which show that black carbon powder derived from scrap rubber can be added to compositions of rubber without compromising the physical properties of the rubber compositions.
[160] The invention will be further elucidated by means of a Drawing explained below. DESIGN
[161] Figure 1 presents a process flowchart for the process according to the invention. DRAWING DESCRIPTION
[162] Figure 1 presents a process flowchart that explains an embodiment of the present invention. This flowchart is not limiting of the present invention, but is for illustrative purposes only.
[163] Granulated raw material tires (scrap rubber) are mixed from two raw material feeders (1) in a raw material mixer (2). The resulting mixed raw material is added to a first rotary kiln (3) in which the at least first stage of pyrolysis a) takes place to obtain an intermediate carbon material. The intermediate carbon material is added to a second oven (polishing oven, 4) to obtain a carbon material according to the present invention.
[164] Volatiles released in the first and at least second pyrolysis stages are collected in the receiving lines (5) and optionally used for steam generation or electricity generation. The condensable volatiles (namely oils) collected from the at least first stage of pyrolysis are condensed in a condenser (7).
[165] Subsequently, the obtained coal material is fed into a coal cooler (8), this coal material is then broken down into a breaking mill (9). A magnetic separator (10) is used to remove any remaining steel components (resulting from the steel reinforcement of raw material tires) before feeding the coal material into a jet milling apparatus (11). The product from the milling step is known as a black carbon powder and is subsequently pelleted in a pelletizer (12). The pelletized black carbon powder is then fed through a fluid bed (13) to produce the final product black carbon powder (14).
[166] The invention should now be exemplified by several non-limiting examples. EXAMPLES
[167] The following examples present several process steps of the present invention. PYROLYSIS
[168] This example shows a rotary kiln that operates in a two-stage pyrolysis mode.
[169] The scrap rubber obtained from tires was added to the pyrolysis apparatus in the form of a granulate, where 100% of the particles have a length of less than 30 mm, a width of less than 25 mm and a height of less than 30 mm, and 95% of the particles have a span of less than 25 mm, have a span of less than 25 mm, and a height of less than 25 mm. The composition of the scrap rubber obtained from raw material tires having a low silica content (A), a medium silica content (B) or a high silica content (C) is shown in Table 1 below. All numbers are in percent by weight, based on the total weight of the scrap rubber.
[170] Table 1 The composition of typical raw material tires is:

[171] Table 2 below reveals the conditions that were used for the pyrolysis of several Examples according to the invention (Examples 1-7) and not according to the invention (Comparative example). Examples 1 and 2 were carried out in two parts, 1A and 1B, and 2A and 2B, respectively. 1A and 2A refer to the first stage of the pyrolysis process, while 1B and 2B refer to the second stage of the pyrolysis process. This was done in order to determine the percentage of volatiles in the intermediate carbon material obtained after the first stage of pyrolysis (1A and 2A).
[172] Table 2 Conditions used for the first and second stage of the pyrolysis step and the volatile content of the product obtained therefrom.

EXAMPLES 1-7 AND COMPARATIVE EXAMPLE 1
[173] An electrically heated rotary stove was configured using a 238 mm (9.38”) cylindrical tube OD, expanded with an integral, internal flight cartridge, no cooling zone, sealed feed support assembly with two ports slides to minimize air infiltration, two heaters that have been installed in series relative to each other to pre-heat the nitrogen gas before entering the feed ducts and cylinder. A two-stage condenser system, after the discharge ducts, was installed to collect the condensable oil that was produced during pyrolysis. A gas totalizer with bypass arrangement was installed in the vent lines downstream of the condenser to obtain periodic measurements of the outward gas flow rate. The oven was adjusted for simultaneous flow. A nitrogen drain was used to maintain an inert atmosphere inside the oven during pyrolysis; the product compartment containers were also purged with nitrogen.
[174] The tire pyrolysis process was carried out in two stages, with the equipment systems as described above. The first stage being the “carbonization” stage, in which 10 kg of feed material was heated to the point of release of volatiles (simultaneous operation) and the oven was rotated at 1-2 rpm; and the second stage being the “polishing and cooling” stage, in which the intermediate carbon material, with a small amount of residual volatile matter remaining, was removed and the oven was rotated at 3-4 rpm. As noted in Table 2 above, for some of the Examples and Comparative Example, the first or second stage of pyrolysis was omitted.
[175] Prior to conducting the test studies, all gas-free breather line system components were weighed and recorded in order to obtain an accurate mass balance of the constituted material for the first stage and the second stage, the stage carbonization of tire pyrolysis. POLYAROMATIC HYDROCARBIDE (PAH) ANALYSIS
[176] The carbon material obtained from the pyrolysis of scrap tires, as described in Examples 6, 7 and Comparative Example 1, was analyzed according to DIN 51720-2001 (volatile content), DIN 51719-1197 (ash content) and DIN ISO 11465-1996 (moisture) and Merkbl. 1, LUA-NRW (GCMSD) (PAH). The material prepared according to the invention (namely Example 6 and Example 7) was compared to the material prepared according to the prior art (Comparative Example 1), which was processed only in the first stage of pyrolysis. Two additional carbon materials were tested, both of which are commercially unavailable products which are denoted Comparative Example 2 (obtained from Carbon Clean Tech, Germany [Germany]) and Comparative Example 3 (obtained from Erus d.o.o., Slovenia [Slovenia]). These Comparative Examples 2 and 3 are both carbon black powders obtained by prior art methods. The composition of the coal materials is given in Table 3 below and the polyaromatic hydrocarbon analysis is given in Table 4 below.
[177] Table 3 Comparison of the carbon material obtained by the invention and the prior art.


[153] Table 4 PAH content for the coal material listed in Table 3

MILLING
[154] The coal materials obtained in Examples 6 and 7 were milled in a Lab AFG 100 milling apparatus (from Hosokawa Alpine). The grinding apparatus was operated at a temperature of 20 °C and 22,000 rpm, using air as the medium, at a pressure of 3 bar, feed was added directly to the grinder through 3 nozzles with a diameter of 1.9 mm .
[155] The milled product was measured for particle size distribution (D50 & D99) using wet laser diffraction in a Malvern Mastersizer S Ver 2.19. The shift lens was 300 RF mm, the beam length was 2.40 mm. The analysis method used was Polydispersion. A mixture, commercially available Morvet® + Supragil® (used in a ratio of 70:30) was used as the wetting agent and external ultrasound was applied to prevent aggregation of the particles. The results obtained are shown in Table 5 and Table 6 below. In Table 6 below, measurements were performed on two commercially available furnace blacks, denoted Comparative Example 4 (Birla Carbon N550) and Comparative Example 5 (Birla Carbon N660).
[156] Table 5 Particle size distribution of ground black carbon powder according to the invention.

[157] Table 6 Particle size distribution and BET surface area of carbon black powder derived from scrap rubber (according to the invention) and furnace black (prior art).
EPDM RUBBER COMPOSITION
[158] Rubber compositions were made by mixing black carbon powder derived from scrap rubber or commercially available furnace derived carbon with an EPDM rubber and other components, as shown in Table 7.
[159] Table 7 Composition of an EPDM rubber comprising black carbon derived from scrap rubber.

[160] The composition of the commercially available rubber used (Keltan) is further elucidated in Table 8 below.
[161] Table 8 Composition of Keltan® 8340A


[162] Measurements of the mechanical properties of rubber compositions are summarized in Table 9 below. Comparative Example 6 is a rubber composition according to Table 7, wherein a carbon black according to Comparative Example 4 is used. Comparative Example 7 is a rubber composition according to Table 7, wherein a carbon black according to Comparative Example 5 is used. Example 8 is a rubber composition according to Table 7, where a carbon black according to Example 2 (after steps 2A and 2B) is used.
[163] Table 9 Mechanical properties of EPDM rubber compositions comprising carbon black carbon and furnace black carbon.
#1: Tensile strength was measured in accordance with ISO 37-2011. #2: M100 was measured, according to ISO 37-2005. #3: M300 was measured, according to ISO 37-2005. #4: Fatigue DeMattia flex was measured, per ASTM D2230-2012. #5: Bouncing Resilience (Schob) was measured in accordance with ISO4662-2009.
[164] The measurements presented in Table 8 clearly show that the EPDM rubber composition of Example 8, according to the present invention, has much lower stiffness modulus M100 and M300, while maintaining tensile strength compared to rubber compositions of prior art.
[165] This combination of properties allows for greater loading of carbon black powders according to the present invention compared to prior art carbon black powders without compromising physical properties. This will result in reduced compounding cost due to increased dilution of the more expensive polymer. SBR RUBBER COMPOSITION
[166] Rubber compositions were made by mixing black carbon powder derived from scrap rubber or commercially available furnace derived carbon with an SBR rubber and other components as shown in Table 10. Rubber compositions were made in accordance with ASTM D3191-2010.
[167] Table 10 SBR rubber compositions


[168] The composition of the commercially available rubber used (SBR 1500) is further elucidated in Table 11 below.
[169] Table 11 The specification of SBR 1500

[170] Measurements on the mechanical properties of rubber compositions are summarized in Table 12 below. Comparative Example 8 is a rubber composition according to Table 9, in which a carbon black according to Comparative Example 4 is used. Comparative Example 9 is a rubber composition according to Table 9, wherein a carbon black according to Comparative Example 5 is used. Example 9 is a rubber composition according to Table 9, wherein a carbon black according to Example 2 (after steps 2A and 2B) is used.
[171] Table 12 Mechanical properties of SBR rubber compositions comprising carbon black carbon and furnace black carbon
#1: Tensile strength was measured in accordance with ISO 37-2011. #2: M100 was measured, in accordance with ISO 37-2005. #3: M300 was measured, according to ISO 37-2005. #4: Elongation was measured, per ISO 372005. #5: Fatigue DeMattia flex was measured, per ASTM D2230-2012. #6: Bouncing Resilience (Schob) was measured in accordance with ISO4662-2009.
[172] Similar to the EPDM rubber compositions reported above, the SBR rubber composition of Example 9, according to the present invention, has much higher M100 and M300 stiffness modulus and a much greater elongation compared to the compositions according to the Comparative Examples, while maintaining the tensile strength.
[173] The composition of Example 9 has a particularly superior combination of mechanical properties over comparative compositions. Comparative example 8 has a high tensile strength, but elongation is low and bending fatigue is especially low. Comparative Example 9 has reasonable elongation and bending fatigue, but tensile strength is low. The composition of Example 9 has good properties in all these respects.
[174] This combination of properties allows for greater loading of carbon black powders according to the present invention, compared to prior art carbon black powders, without compromising physical properties. ZnO ACTIVITY IN BLACK CARBON POWDER DERIVED FROM SCRAP RUBBER
[175] In order to assess zinc oxide (ZnO) activity, several tests were performed. Zinc oxide has an effect on crosslink density. Preferably, the lowest amount of ZnO that will still give maximum crosslink density is used. In other words, it is preferred to keep the amount of ZnO as low as possible. Therefore, a black carbon that provides maximum crosslink density in a low amount of ZnO is sought.
[176] Rubber compositions comprising SBR 1500 (ASTM D3191-2010), a carbon black powder (from Example 2 or Comparative Example 4) and various amounts of zinc oxide were made and vulcanized. From the result of this, the amount of ZnO at which the maximum crosslink density was obtained was determined.
[177] A rubber composition comprising carbon black, according to Comparative Example 4, exhibited a maximum crosslink density at 3% by weight of added ZnO.
[178] The composition comprising the carbon black powder of Example 2 had a maximum crosslink density at 1.5% by weight of added ZnO.
[179] An increase in added ZnO to 3% by weight did not give a further increase in crosslink density.
[180] From these experiments, it can be deduced that less ZnO is needed when carbon black according to the present invention is used, compared to the prior art. The present inventors believe, without wishing to be bound by any theory, that carbon black, according to the present invention, already comprises a certain amount of ZnO, so that the addition of extra ZnO during rubber composition can be reduced significantly, which is a benefit of the present invention.
[181] The above experiments clearly present that one or more objects of the present invention are achieved by the embodiments mentioned above and in the appended claims.

权利要求:
Claims (15)
[0001]
1. METHOD FOR RECYCLING A SCRAP RUBBER, IN PARTICULAR TIRES, said method comprising the following steps: i) pyrolysis of a scrap rubber to obtain a coal material; j) ) grinding the carbon material obtained in step i) to obtain a black carbon powder; characterized by pyrolysis, in step i), comprises at least a two-stage pyrolysis process, wherein said two-stage pyrolysis process comprises: k) a first pyrolysis stage to obtain an intermediate carbon material, and l) a second stage of pyrolysis to obtain a coal material, wherein the first stage a) is carried out in a first rotary kiln, where the temperature during the first stage of pyrolysis a) is between 500 - 800°C, and temperature during the second pyrolysis stage b) is between 550 - 800°C, the temperature during the second pyrolysis stage b) being higher than the temperature of the first pyrolysis stage a).
[0002]
2. METHOD according to claim 1, characterized in that in the at least first stage of pyrolysis a) the percentage of volatiles present in said scrap rubber is reduced to an amount of 5-10% by weight based on the total weight of the intermediate carbon material, wherein the intermediate carbon material is introduced to the second stage of pyrolysis b) in which the percentage of volatiles is further reduced to a percentage of less than 2.5% by weight, preferably less than 2.0% by weight, based on the total weight of the carbon material, wherein a continuous flow of gas flowing through the rotary kiln used in at least one of the recited stages a) and b).
[0003]
3. METHOD according to any one of claims 1 to 2, characterized in that the temperature during the first pyrolysis stage a) is 600-700 °C and preferably 630-670 °C, and the temperature during the second pyrolysis stage b ) be between 650-750 °C and preferably 680-720 °C.
[0004]
4. METHOD according to any one of claims 1 to 3, characterized in that the temperature in the second stage of pyrolysis b) is at least 30°C, preferably at least 50°C, more preferably at least 80°C higher than in the first stage of pyrolysis a).
[0005]
5. METHOD according to any one of claims 1 to 4, characterized in that the residence time of each of the first pyrolysis stage a) and the second pyrolysis stage is independently between 20-50 minutes, preferably 25-45 minutes, and more preferably 3040 minutes, and preferably the residence time of each of the first pyrolysis stage a) and the second pyrolysis stage b) is equal in duration.
[0006]
6. METHOD according to any one of claims 1 to 5, characterized in that in the second stage of pyrolysis b) the percentage of volatiles is reduced to less than 1.0% by weight based on the total weight of the charcoal material.
[0007]
7. METHOD, according to any one of the preceding claims, characterized in that the milling of step ii) is carried out so that the black carbon powder, obtained from step ii), has a particle size distribution of D50<10 µm and D99<40 µm, preferably a particle size distribution of D50<5 µm and D99<20 µm, more preferably a particle size distribution of D50<1 µm and D99<10 µm, even more preferably a size distribution of particle of D50<0.5 μm and D99<2 μm.
[0008]
8. METHOD according to any one of the preceding claims, characterized in that an additional pelletizing step (step iii)) is performed after step ii), wherein the pelletizing of step iii) is performed by mixing a binding agent with the black carbon powder obtained in step ii) and pelletizing the mixture thus obtained to obtain a pelletized black carbon powder.
[0009]
9. METHOD according to any one of the preceding claims, characterized in that the rotary kiln is a cylindrical container, gently tilted to the horizontal, which rotates on its axis, in which the material to be processed is fed by the upper end of the cylinder and gradually moves down towards a lower end as the stove rotates.
[0010]
10. BLACK CARBON POWDER DERIVED FROM SCRAP RUBBER, obtained by the process described in claim 1, wherein the black carbon powder derived from scrap rubber is characterized by comprising: a) 60-98% by weight of black carbon, b ) less than 2.0% by weight of volatiles, c) 0-30% by weight of silica. and has a polyaromatic hydrocarbon (HPA) content of less than 0.25 mg/kg.
[0011]
11. BLACK CARBON POWDER DERIVED FROM SCRAP RUBBER, according to claim 10, characterized in that black carbon powder derived from scrap rubber has a polyaromatic hydrocarbon (HPA) content less than 0.25 mg/kg, plus preferably less than 0.01 mg/kg.
[0012]
12. BLACK CARBON POWDER DERIVED FROM SCRAP RUBBER, according to any one of claims 10 to 11, characterized in that it further comprises zinc oxide in an amount of 1 to 5% by weight, based on the total weight of the black carbon powder , and/or zinc sulfide in an amount of 1 to 5% by weight, based on the total weight of the black carbon powder, wherein the ratio of zinc oxide to said zinc sulfide is between 1:10 to 10 :1, preferably between 1:2 and 2:1.
[0013]
13. BLACK CARBON POWDER DERIVED FROM SCRAP RUBBER, according to any one of claims 10 to 12, characterized in that it has a BET surface area of at least 60 m2/g, preferably at least 70 m2/g and even more preferably a BET surface area of at least 75 m2/g, have an STSA (Statistical Thickness Surface Area) between 46-86 m2/g, preferably 59-79 m2/g, even more preferably 64-74 m2/g, have an oil absorption number between 67-97 m3/g, preferably between 7292 m3/g, more preferably between 77-87 m3/g, and having a primary particle size between 20-40 nm, preferably between 26-36 nm , more preferably between 28-34 nm.
[0014]
BLACK CARBON GRANULE PELLED DERIVED FROM SCRAP RUBBER, comprising a black carbon powder derived from scrap rubber as defined in any one of claims 10 to 13 and a binding agent, characterized in that the amount of binding agent is 0.5 to 1.0% by weight.
[0015]
15. USE OF A BLACK CARBON POWDER DERIVED FROM SCRAP RUBBER, as defined in any one of claims 10 to 13, or obtained according to the method defined in any one of claims 1 to 9, characterized in that it is an excipient or of reinforcement in a rubber composition, a paint, a paint, a putty, a thermoplastic composition or a thermoplastic elastomer.

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同族专利:

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公开号 | 公开日

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US20170114222A1|2017-04-27|

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CN104125988A|2014-10-29|

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EP2794766A1|2014-10-29|

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PL2794766T3|2018-09-28|

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BR112014014978A2|2017-06-13|

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US9580606B2|2017-02-28|

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WO2013095145A1|2013-06-27|

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US10119031B2|2018-11-06|

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EP2794766B1|2018-04-04|

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CN104125988B|2016-01-27|

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US20140371385A1|2014-12-18|

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ES2675128T3|2018-07-06|

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法律状态:
2018-03-27| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|

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2019-08-20| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|

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2020-12-29| B06A| Notification to applicant to reply to the report for non-patentability or inadequacy of the application [chapter 6.1 patent gazette]|

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2021-03-02| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

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2021-05-11| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 21/12/2012, OBSERVADAS AS CONDICOES LEGAIS. |

优先权:

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申请号 | 申请日 | 专利标题

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EP11195394.9|2011-12-22|

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EP11195394|2011-12-22|

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PCT/NL2012/050919|WO2013095145A1|2011-12-22|2012-12-21|A method for obtaining a carbon black powder by pyrolyzing scrap rubber, the carbon black thus obtained and the use thereof|

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