WO2004094513A1 - Rubber reduction - Google Patents
Rubber reduction Download PDFInfo
- Publication number
- WO2004094513A1 WO2004094513A1 PCT/CA2003/001421 CA0301421W WO2004094513A1 WO 2004094513 A1 WO2004094513 A1 WO 2004094513A1 CA 0301421 W CA0301421 W CA 0301421W WO 2004094513 A1 WO2004094513 A1 WO 2004094513A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- rubber
- solvent
- temperature
- tire
- hydrocarbon
- Prior art date
Links
- 229920001971 elastomer Polymers 0.000 title claims abstract description 119
- 239000005060 rubber Substances 0.000 title claims abstract description 119
- 230000009467 reduction Effects 0.000 title claims description 10
- 238000000034 method Methods 0.000 claims abstract description 88
- 239000002904 solvent Substances 0.000 claims abstract description 67
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 59
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 59
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 56
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 28
- 239000007790 solid phase Substances 0.000 claims abstract description 19
- 229920003051 synthetic elastomer Polymers 0.000 claims abstract description 16
- 239000005061 synthetic rubber Substances 0.000 claims abstract description 14
- 229920006395 saturated elastomer Polymers 0.000 claims abstract description 12
- 239000004636 vulcanized rubber Substances 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 230000008569 process Effects 0.000 claims description 45
- 239000006229 carbon black Substances 0.000 claims description 35
- 239000000203 mixture Substances 0.000 claims description 13
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 10
- 239000005864 Sulphur Substances 0.000 claims description 10
- 239000003960 organic solvent Substances 0.000 claims description 6
- 238000013459 approach Methods 0.000 claims description 4
- 238000004090 dissolution Methods 0.000 claims description 4
- 239000011261 inert gas Substances 0.000 claims description 4
- 238000005406 washing Methods 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 125000003158 alcohol group Chemical group 0.000 claims 1
- 239000002245 particle Substances 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 34
- 239000003921 oil Substances 0.000 description 17
- 238000011946 reduction process Methods 0.000 description 15
- 238000012545 processing Methods 0.000 description 13
- 238000000197 pyrolysis Methods 0.000 description 12
- 239000007787 solid Substances 0.000 description 10
- 244000043261 Hevea brasiliensis Species 0.000 description 8
- 229920003052 natural elastomer Polymers 0.000 description 8
- 229920001194 natural rubber Polymers 0.000 description 8
- 230000035484 reaction time Effects 0.000 description 7
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 description 6
- 238000000926 separation method Methods 0.000 description 5
- 229920003048 styrene butadiene rubber Polymers 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 4
- 239000000470 constituent Substances 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 239000002174 Styrene-butadiene Substances 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000001298 alcohols Chemical class 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000010926 purge Methods 0.000 description 3
- 238000000638 solvent extraction Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 241000872198 Serjania polyphylla Species 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229920002857 polybutadiene Polymers 0.000 description 2
- 238000010058 rubber compounding Methods 0.000 description 2
- ROGIWVXWXZRRMZ-UHFFFAOYSA-N 2-methylbuta-1,3-diene;styrene Chemical compound CC(=C)C=C.C=CC1=CC=CC=C1 ROGIWVXWXZRRMZ-UHFFFAOYSA-N 0.000 description 1
- 229920002209 Crumb rubber Polymers 0.000 description 1
- 239000004606 Fillers/Extenders Substances 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- 229920005683 SIBR Polymers 0.000 description 1
- XAQHXGSHRMHVMU-UHFFFAOYSA-N [S].[S] Chemical compound [S].[S] XAQHXGSHRMHVMU-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- -1 bromobutyl Chemical group 0.000 description 1
- 229920005557 bromobutyl Polymers 0.000 description 1
- VLLYOYVKQDKAHN-UHFFFAOYSA-N buta-1,3-diene;2-methylbuta-1,3-diene Chemical compound C=CC=C.CC(=C)C=C VLLYOYVKQDKAHN-UHFFFAOYSA-N 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229920005556 chlorobutyl Polymers 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- 238000012691 depolymerization reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000005227 gel permeation chromatography Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000002085 irritant Substances 0.000 description 1
- 231100000021 irritant Toxicity 0.000 description 1
- 229920003049 isoprene rubber Polymers 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 238000012667 polymer degradation Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002296 pyrolytic carbon Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
- C08J11/14—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with steam or water
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
- C08J11/18—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material
- C08J11/22—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic oxygen-containing compounds
- C08J11/24—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation by treatment with organic material by treatment with organic oxygen-containing compounds containing hydroxyl groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2321/00—Characterised by the use of unspecified rubbers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Definitions
- the invention generally relates to rubber reduction, and more particularly to rubber reduction using solvent extraction techniques at a subcritical temperature.
- Another group of reclamation methods look to extracting increased value from the constituent materials within a tire.
- the major constituents include synthetic and natural rubber, carbon black and steel and minor constituents include sulphur and any stabilizers.
- the processes within this group may be referred to as reduction processes where the tire is being reduced to its constituents.
- LeBeau discusses the reclamation of rubber that includes styrene- butadiene rubber (SBR), a synthetic rubber, using steam in Science and Technology of Reclaimed Rubber, Rubber Chemistry and Technology 40, 1967, 217-237.
- Figure 1 Figure 1 of LeBeau, illustrates effect of steam treatment on natural rubber and SBR. Natural rubber softens i.e. the viscosity is lowered and can be reclaimed when exposed to 200 psi steam. However, SBR experiences a short-lived softening that is followed by an extended hardening. LeBeau notes that the rate of hardening increases with increasing temperature. LeBeau further notes that the reclamation of synthetic rubbers therefore requires reclaiming agents or catalysts.
- SBR styrene- butadiene rubber
- One process used for the reduction of used tires that include synthetic rubbers is pyrolysis.
- the tires are subjected to temperatures between 600 and 900°C in either an inert atmosphere or a vacuum. This process produces light oils and char where the char contains carbon black and pyrolytic carbon formed by the carbonization of rubber hydrocarbon.
- Pyrolysis is generally not seen as a desirable reduction process. With the rubber hydrocarbons being either reduced to light oils or carbonized to char the end products of a pyrolysis process do not retain much of the economic value associated with the original rubber hydrocarbon and carbon black.
- Reduction processes typically include devulcanization and depolymerization steps or processes.
- the devulcanization process breaks sulphur-sulphur and sulphur-carbon bonds that cross-link rubber molecules.
- the devulcanization process produces a solid residue where the mass of the solid residue is approximately 100% of the original mass of tire.
- the solid residue contains rubber hydrocarbon and carbon black where rubber hydrocarbon includes any hydrocarbon with a molecular weight above that of oil that originates from the initial rubber.
- the rubber hydrocarbon has an average molecular weight that is generally less than the initial rubber but much greater than oil, where oil has an average molecular weight of approximately 500 or less.
- the depolymerization process reduces the average molecular weight of the rubber hydrocarbon by breaking carbon-carbon bonds of the rubber hydrocarbon until, at completion, the rubber hydrocarbon has been reduced to oil.
- the depolymerization process at completion, reduces the molecular weight from around 200,000 to 500.
- the mass of solid residue is approximately 40% of the initial mass of tire. At this point the solid residue is substantially only carbon black with the rubber hydrocarbon being completely reduced to oil.
- Figure 2a is schematic graph of the % completion v. time for a typical pyrolysis process.
- a devulcanization process 202 and a depolymerization process 204 occur substantially in parallel. As such the two processes are complete at approximately the same time i.e. t v ⁇ t p .
- Figure 2b shows a non-pyrolysis process in which the devulcanization process 206 is separated from the depolymerization process 208.
- the devulcanization process 206 is complete while the depolymerization process 208 is only a fraction of the way to completion.
- Solvent extraction uses elevated temperatures and pressures in the presence of a solvent to at least devulcanize and often depolymerize the rubber. In almost all of the work in this area processing is conducted at a temperature and pressure that are above the critical values of these parameters for the particular solvent in which processing is being conducted.
- Supercritical reaction conditions are defined as having a reaction temperature that is above the critical temperature and a pressure that is above the critical pressure. Supercritical reactions have been performed using a variety of solvents including alcohols, organic solvents and water. Much of the work using supercritical reaction conditions has been directed to extensive depolymerization of the rubber. In particular work has been directed to the reduction of the rubber to oil. Supercritical processing has been found to be advantageous in these cases as it provides a feasible reaction rate for the required depolymerization reactions. However, as the resulting oil will generally be used as a fuel the economic value of the rubber is reduced to a level well below that of that imparted to the tire during initial processing.
- 2-butanol is flammable, has a low flash point and is an irritant.
- the invention is directed to a method for the reduction of rubber.
- An object of the invention is to mitigate one or more disadvantages in the prior art.
- a further object of the invention is to provide a method for the reduction of rubber that includes synthetic rubber using a solvent that includes water where at least a portion of reaction product has a molecular weight that is larger than oils.
- a method of reducing vulcanized rubber comprises the steps of heating the rubber, wherein the rubber includes synthetic rubber, in the presence of a solvent, wherein the solvent includes water to a temperature below a critical temperature of the solvent, providing a pressure that is at least equal to a saturated vapour pressure of the solvent at the temperature, and maintaining the temperature and the pressure for a time sufficient to devulcanize the rubber and produce a reaction product that is primarily a solid phase and includes rubber hydrocarbon.
- a method of reducing a vulcanized tire comprises the steps of heating the tire, wherein the tire includes synthetic rubber, in the presence of a first solvent, wherein the first solvent includes water, to a temperature below a critical temperature of the first solvent, providing a pressure that is at least equal to a saturated vapour pressure of the solvent at the temperature, maintaining the temperature and the pressure for a time sufficient to devulcanize the tire and produce a reaction product that is primarily a solid phase and includes rubber hydrocarbon, washing and drying the solid phase of the reaction product, dissolving the rubber hydrocarbon in a second solvent, the second solvent being appropriate for the dissolution of rubber hydrocarbon therein, separating the carbon black from the reaction product and separating the second solvent from the rubber hydrocarbon.
- Figure 1 is a schematic diagram of viscosity v. time for natural rubber and SBR;
- Fig. 2a is a schematic graph illustrating % completion v. time for a pyrolysis reduction process
- Fig. 2b is a schematic graph illustrating % completion v. time for a non- pyrolysis reduction process
- Fig. 3 is a schematic graph of mass of solid residue vs. stages of reduction process
- Fig. 4 is a flow chart of a process for reducing tires according to an embodiment of the invention.
- Fig. 5 is a flow chart of a process for reducing tires according to another embodiment of the invention.
- Fig. 6 is a flow chart of a process for reducing tires according to a further embodiment of the invention.
- Like numerals identify like features within the drawings.
- An embodiment of the current invention provides a method for the reduction of rubber using subcritical water i.e. the reduction process occurs at a temperature below the critical temperature of water.
- critical temperature of water as used herein is defined as the temperature above which steam cannot be liquefied by the application of pressure.
- the critical temperature of water is 374°C.
- Process parameters for subcritical fluid techniques include pressure, temperature, solvent and time. Without being bound by theory it appears that operation of the process at temperatures below the critical temperature of the solvent allows for the separation of the devulcanization and the depolymerization processes. The rate of depolymerization process is lowered to an extent where it is effectively separated from the step of devulcanization. This allows improved control regarding the extent to which depolymerization is allowed to proceed.
- the reaction time and temperature are varied to provide substantially complete devulcanization and a desired amount of depolymerization.
- Figure 3 presents a schematic graph of mass of solid residue v. stages in the tire reduction process.
- a line 302 represents a non-pyrolysis process while a line 312 represents a typical pyrolysis process.
- the line 312 i.e. a typical pyrolisis process is complete at a point 314 where rubber hydrocarbon have been reduced to light oils and some has been carbonized to char.
- the line 302 contains a devulcanization portion 304 and a depolymerization portion 308.
- the initial rubber has undergone substantially 100 % devulcanization.
- the mass of solid residue is essentially 100 % with the solid residue containing rubber hydrocarbon and carbon black.
- the average molecular weight of the rubber hydrocarbon is reduced.
- the rubber hydrocarbon is substantially a mixture of oils and carbon black, where the oils generally have average molecular weights of less than about 500.
- the solid residue at the end of the depolymerization process i.e. at a point 310 is substantially carbon black.
- the variance between the points 310 and 314 represents the formation of char in the pyrolysis process.
- Rubber feedstock is provided to a reactor suitable for temperatures and pressures appropriate for subcritical treatment with a solvent at step 402.
- the rubber feedstock may be any vulcanized rubber that includes synthetic rubber.
- Typical synthetic rubbers include synthetic polyisoprene rubber, polybutadiene rubber, styrene-butadiene rubber, isoprene-butadiene rubber, styrene- isoprene rubber, styrene-isoprene-butadiene rubber, nitrile rubber, bromobutyl rubber and chlorobutyl rubber.
- the above list of rubbers is not meant to be limiting. Other appropriate rubbers will, upon consideration of the above list, be apparent to one of skill in the art.
- the rubber feedstock is used automobile tires.
- the automobile tires used as rubber feedstock are shredded.
- the shredding process produces pieces or rubber with anisotropic dimensions.
- the pieces are between about 1 and about 4 mm thick and had a surface area of between about 0.5 and about 5 cm 2 .
- the pieces are more typically between about 1 and about 2 mm thick and have a surface area of between about 1 and about 2 cm 2 .
- the rubber feedstock has been shredded in the above embodiment the invention is by no means limited to a particular size of rubber feedstock.
- the method of the invention can also be applied to whole tires.
- the method of the invention is independent of the size of rubber feedstock.
- a solvent is provided to the reactor at step 404.
- the solvent is water.
- the amount of solvent provided is sufficient to provide the saturated solvent vapour pressure at the reaction temperature while maintaining some solvent in the reactor.
- the solvent within the reactor is sufficient for the tire feedstock to be immersed in the solvent at the reaction temperature and remains so for the duration of the reduction process.
- the rubber feedstock is placed in a basket such that the rubber is above the level of the solvent for the duration of the reduction process.
- the reactor is heated to the reaction temperature, T, at step 406. To maintain a subcritical reaction the reaction temperature must be less than the critical temperature of the solvent. In the current exemplary embodiment the temperature is less than 374°C. In an embodiment of the invention the reaction temperature is preferably between about 260°C and about 370°C. The reaction temperature is more preferably between about 290°C and about 320°C.
- air present in the reactor Prior to attaining the desired reaction temperature air present in the reactor is purged.
- the air present in the reactor is purged with steam generated during the heating step.
- Other appropriate means for purging air from the reactor including purging with an inert gas, will be apparent to those of skill in the art.
- a pressure is provided to the reactor at step 408. This pressure is equal to or greater than the saturated solvent vapour pressure at the reaction temperature.
- the reaction pressure is the saturated water vapour pressure at the reaction temperature. This pressure is solely created by steam present in the reactor. For example, for a reaction temperature of 300°C the pressure is 1230 psig.
- pressures greater than the saturated solvent vapour pressure are provided by the application of an inert gas to the reaction chamber. Inert gases appropriate for this pressurization of the reactor include, but are not limited to, nitrogen and argon. Other means of providing pressures above the saturated water vapour pressure will be apparent to those of skill in the art. The use of means to provide a pressure that are independent of the generation of vapour allows control of the fraction of vapour present in the reactor.
- the reaction is continued at step 410 for time t to produce a reaction product.
- the reaction product produced according to the method of the current exemplary embodiment of the invention includes rubber hydrocarbon, carbon black and sulphur.
- the reaction product may also include, depending on the exact reaction parameters, oil from at least partial depolymerization of the rubber hydrocarbon, and vulcanized rubber feedstock.
- the reaction product can generally be divided into a solid and liquid phase.
- the solid phase contains the rubber hydrocarbon, carbon black and any vulcanized rubber.
- the liquid phase contains any oil that is produced.
- the liquid phase will be present as a slurry with the water. While not being limited by theory it is believed sulphur is dissolved in the water during the reaction. The sulphur then precipitates from the water upon cooling and is deposited on the solid phase.
- a flow chart of a reduction process according to another embodiment of the invention is presented in Figure 5.
- the process includes the steps presented in Figure 4.
- the process according to this embodiment of the invention further includes the washing and drying the solid phase at step 501.
- the solid phase is washed with water.
- the solid phase of the reaction product is treated with a solvent.
- this solvent is cyclohexane.
- the use of other solvents appropriate for the dissolution of rubber hydrocarbon, including toluene, is also within the scope of the invention.
- the use of other solvents and mixtures of solvents as appropriate for the dissolution of the rubber hydrocarbon, which may include hydrocarbons of varying molecular weight will be apparent to one skilled in the art.
- Carbon black is then separated at step 504 using filtration methods. It will be apparent to one skilled in the art that any appropriate techniques may be implemented for the separation of the carbon black form the dissolved reaction product. It will also be apparent that step 504 may be omitted for those rubber feedstocks that do not include carbon black.
- a flow chart of a reduction process according to a further embodiment of the invention is presented in Figure 6.
- the process includes the steps presented in Figure 5.
- the process according to this embodiment of this invention further includes the step of separating the solvent from the rubber hydrocarbon. Techniques appropriate for separating the solvent from the rubber hydrocarbon will be apparent to one skilled in the art. In this embodiment evaporation is used to separate the solvent from the rubber hydrocarbon.
- the extraction solvent is a mixture of solvents, where the mixture includes water such that the water plays a role in the extraction/ devulcanization process.
- mixtures of solvents that included 10 weight percent and 30 weight percent ethanol in water were used in reduction processes conducted at temperatures of 280°C, and 290°C and above. It was found that the % devulcanization was approximately the same when using the mixed solvent compared to 100% water. It is contemplated that alcohols and organic solvents are applicable for mixture with water to form the extraction solvent.
- the rubber feedstock was from used automobile tires.
- the tires were processed to remove any steel and fibre belts contained therein.
- the rubber was shredded to produce chips or shavings having an irregular shape.
- the chips and shavings were generally between about 1 and about 4 mm thick and had a surface area of between about 0.5 to about 5 cm 2 .
- the majority of chips and shavings were between about 1 and about 2 mm thick and had a surface area of between about 1 to about 2 cm 2 .
- a reactor capable of operating at temperatures of up to 500°C and pressures of up to 5000 psi was used in all experiments.
- the reactor was charged with between about 20 and about 30 g of rubber and about 100 ml of water. In most experiments the rubber sample was immersed in water in the reactor. In some experiments the rubber sample was held in a perforated basket above the water. Heating was initiated with a valve on the reactor remaining open. This valve was closed after the vessel had reached a temperature greater than 100°C. This allowed for the purging of air from the reactor with steam generated during heating of the reactor. The temperature was raised to the desired reaction temperature and the reaction continued for either one or five hours. At the end of the desired reaction time the reactor was cooled to room temperature and the contents removed.
- the nature and relative amount of reaction products present at the end of a reaction are a function of the particular reaction conditions.
- the reaction products may include vulcanized rubber, rubber hydrocarbon, oil and carbon black.
- the vulcanized rubber, rubber hydrocarbon and carbon black were present in a solid phase while the oil was present in a liquid phase.
- the solid phase was washed with water and dried to constant weight in an oven at 100°C. This washing step removed any sulphur that was on the reaction product.
- the yield of the rubber reduction process of examples 1-14 is presented in Table 1. The yield (%) is defined by the following expression
- the rubber hydrocarbon of examples 6, 8 and 9 was analysed for sulphur content.
- the sulphur content of the rubber hydrocarbon was 0.19, 0.18 and 0.22% for examples 6, 8 and 9, respectively. Therefore, the measured sulphur content is lower than that of the rubber feedstock indicating that sulphur is extracted from the rubber.
- a multi-step separation process was used to separate the various components of the solid phase.
- the solid phase was mixed with cyclohexane, heated to and held at 60°C and stirred for up to 1 hour. During this process the rubber hydrocarbon dissolved in the cyclohexane.
- the mixture was passed through a wire mesh strainer to remove any vulcanized rubber, which would not be dissolved by the cyclohexane. Any vulcanized rubber that was removed during this filtering step was weighed and the mass compared to the initial mass of rubber. The fraction of the sample that was devulcanized was calculated as a percentage. The results are presented in Table 2.
- the mixture that passed through the strainer was passed through filter paper to separate out the carbon black.
- the extracted carbon black was characterized by measuring its surface area. Nitrogen adsorption on the carbon black was measured at 77°K and a BET equation was used to quote a surface area. A surface area of 60m 2 /g measured for the carbon black of Example 8. The extracted carbon black approaches that used in the manufacture of tires.
- end products could be obtained directly from the reactor without subsequent separation.
- the reaction product will have a carbon black to rubber hydrocarbon ratio that is approximately equal to that of the original rubber.
- the reaction product can be used as an extender for rubber formulations.
- the end product could be rubber hydrocarbon extracted from the reaction product and has had its carbon black removed. It is further possible to set the reaction conditions to tailor the molecular weight of the rubber hydrocarbon.
- the carbon black that has been isolated from the rubber hydrocarbon can be isolated as an end product.
- a low temperature reaction could be used to produce surface modified crumb rubber.
- tires can include any vulcanized rubber tire as may be used for transportation purposes. It will also be apparent to one of skill in the art that other vulcanized rubber products that include synthetic rubber may be used as a feedstock.
- processing conditions presented above are with respect to one embodiment of the invention.
- the invention encompasses those processing parameters i.e. temperature, pressure, time that allow for subcritical processing of rubber with a solvent that includes water.
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SI200332013T SI1618140T1 (en) | 2003-04-22 | 2003-09-18 | Rubber reduction |
AU2003266892A AU2003266892B2 (en) | 2003-04-22 | 2003-09-18 | Rubber reduction |
DK03747773T DK1618140T3 (en) | 2003-04-22 | 2003-09-18 | Reduction of rubber |
AT03747773T ATE514737T1 (en) | 2003-04-22 | 2003-09-18 | REDUCTION OF RUBBER |
MXPA05011337A MXPA05011337A (en) | 2003-04-22 | 2003-09-18 | Rubber reduction. |
BR0318265A BR0318265B1 (en) | 2003-04-22 | 2003-09-18 | Method for reducing vulcanized rubber, superficially devulcanized rubber, completely devulcanized rubber, Method for reducing vulcanized tire, rubber hydrocarbon and carbon black. |
EP20030747773 EP1618140B1 (en) | 2003-04-22 | 2003-09-18 | Rubber reduction |
JP2004571016A JP4708033B2 (en) | 2003-04-22 | 2003-09-18 | Rubber reduction |
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CA 2426253 CA2426253A1 (en) | 2003-04-22 | 2003-04-22 | Rubber reduction |
CA2,426,253 | 2003-04-22 |
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WO2004094513A1 true WO2004094513A1 (en) | 2004-11-04 |
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PCT/CA2003/001421 WO2004094513A1 (en) | 2003-04-22 | 2003-09-18 | Rubber reduction |
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US (1) | US7166658B2 (en) |
EP (1) | EP1618140B1 (en) |
JP (1) | JP4708033B2 (en) |
CN (1) | CN100375758C (en) |
AT (1) | ATE514737T1 (en) |
AU (1) | AU2003266892B2 (en) |
BR (1) | BR0318265B1 (en) |
CA (1) | CA2426253A1 (en) |
CY (1) | CY1111794T1 (en) |
DK (1) | DK1618140T3 (en) |
ES (1) | ES2367017T3 (en) |
MX (1) | MXPA05011337A (en) |
PT (1) | PT1618140E (en) |
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Cited By (4)
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EP2346934A1 (en) * | 2008-10-31 | 2011-07-27 | Brian H. Harrison | Separating devulcanized rubber |
CN101443105B (en) * | 2006-03-27 | 2012-05-02 | 鲁布雷科股份有限公司 | Reactor and reactor system for high temperature and high pressure reactions |
EP2925810A4 (en) * | 2012-11-27 | 2016-07-06 | Brian H Harrison | Vulcanized rubber conversion |
WO2019030701A1 (en) | 2017-08-10 | 2019-02-14 | Avonisys Ag | Method for rubber removal from vulcanization molds |
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US7626062B2 (en) * | 2007-07-31 | 2009-12-01 | Carner William E | System and method for recycling plastics |
FR2946054B1 (en) * | 2009-06-02 | 2012-09-28 | Alfyma Ind | PROCESS FOR TRANSFORMING RUBBER GRANULATES TO PRODUCE SEMI-ACTIVE CARBONIZATION AND PLASTICIZER |
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WO2012021891A2 (en) | 2010-08-13 | 2012-02-16 | Tufts University | Compositions, kits and methods for treatment of complement-related disorders |
CN103073741B (en) * | 2012-12-26 | 2015-02-18 | 南京工业大学 | Method for inducing desulfurization reaction of vulcanized rubber powder through stress of subcritical water extrusion method |
CN104924488A (en) * | 2015-03-28 | 2015-09-23 | 安徽微威胶件集团有限公司 | Manufacturing technology of engine rubber pad |
US10087301B2 (en) | 2015-07-10 | 2018-10-02 | Rubreco Inc. | Dewatering devulcanized rubber |
WO2019023792A1 (en) * | 2017-07-31 | 2019-02-07 | Rubreco Inc. | Vent cleaning of rubber molds |
CN110591149A (en) * | 2019-09-05 | 2019-12-20 | 江苏睿博环保设备有限公司 | Method for desulfurizing vulcanized rubber powder by only using water as auxiliary agent |
CN112917740A (en) * | 2021-01-28 | 2021-06-08 | 张春瑞 | Waste rubber retrieves with soft processing apparatus of thermally equivalent |
EP4116336A1 (en) | 2021-07-09 | 2023-01-11 | The Goodyear Tire & Rubber Company | Rubber product devulcanization method and product |
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- 2003-09-18 CN CNB038264951A patent/CN100375758C/en not_active Expired - Fee Related
- 2003-09-18 AT AT03747773T patent/ATE514737T1/en active
- 2003-09-18 JP JP2004571016A patent/JP4708033B2/en not_active Expired - Fee Related
- 2003-09-18 ES ES03747773T patent/ES2367017T3/en not_active Expired - Lifetime
- 2003-09-18 US US10/666,976 patent/US7166658B2/en active Active
- 2003-09-18 DK DK03747773T patent/DK1618140T3/en active
- 2003-09-18 MX MXPA05011337A patent/MXPA05011337A/en active IP Right Grant
- 2003-09-18 PT PT03747773T patent/PT1618140E/en unknown
- 2003-09-18 AU AU2003266892A patent/AU2003266892B2/en not_active Ceased
- 2003-09-18 BR BR0318265A patent/BR0318265B1/en not_active IP Right Cessation
- 2003-09-18 SI SI200332013T patent/SI1618140T1/en unknown
- 2003-09-18 WO PCT/CA2003/001421 patent/WO2004094513A1/en active Application Filing
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101443105B (en) * | 2006-03-27 | 2012-05-02 | 鲁布雷科股份有限公司 | Reactor and reactor system for high temperature and high pressure reactions |
EP2346934A1 (en) * | 2008-10-31 | 2011-07-27 | Brian H. Harrison | Separating devulcanized rubber |
EP2346934A4 (en) * | 2008-10-31 | 2013-02-27 | Rubreco Inc | Separating devulcanized rubber |
AU2009310582B2 (en) * | 2008-10-31 | 2014-03-06 | Rubreco Inc. | Separating devulcanized rubber |
EP2925810A4 (en) * | 2012-11-27 | 2016-07-06 | Brian H Harrison | Vulcanized rubber conversion |
AU2013351881B2 (en) * | 2012-11-27 | 2017-03-16 | Brian H. Harrison | Vulcanized rubber conversion |
WO2019030701A1 (en) | 2017-08-10 | 2019-02-14 | Avonisys Ag | Method for rubber removal from vulcanization molds |
Also Published As
Publication number | Publication date |
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JP4708033B2 (en) | 2011-06-22 |
ATE514737T1 (en) | 2011-07-15 |
JP2006524266A (en) | 2006-10-26 |
MXPA05011337A (en) | 2006-03-08 |
BR0318265A (en) | 2006-05-23 |
ES2367017T3 (en) | 2011-10-27 |
CN1771286A (en) | 2006-05-10 |
US7166658B2 (en) | 2007-01-23 |
BR0318265B1 (en) | 2013-05-14 |
US20040214906A1 (en) | 2004-10-28 |
CN100375758C (en) | 2008-03-19 |
PT1618140E (en) | 2011-08-01 |
EP1618140A1 (en) | 2006-01-25 |
SI1618140T1 (en) | 2011-10-28 |
AU2003266892A1 (en) | 2004-11-19 |
CA2426253A1 (en) | 2004-10-22 |
AU2003266892B2 (en) | 2010-06-03 |
DK1618140T3 (en) | 2011-07-25 |
EP1618140B1 (en) | 2011-06-29 |
CY1111794T1 (en) | 2015-10-07 |
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