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WO2004044042A1 - Waste collecting method, waste collecting apparatus, volume reducing or softening solution, waste collecting system, waste recycling method, and classified waste collecting method - Google Patents

Waste collecting method, waste collecting apparatus, volume reducing or softening solution, waste collecting system, waste recycling method, and classified waste collecting method Download PDF

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Publication number
WO2004044042A1
WO2004044042A1 PCT/JP2003/014127 JP0314127W WO2004044042A1 WO 2004044042 A1 WO2004044042 A1 WO 2004044042A1 JP 0314127 W JP0314127 W JP 0314127W WO 2004044042 A1 WO2004044042 A1 WO 2004044042A1
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Prior art keywords
solution
volume
plastic
waste
waste material
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PCT/JP2003/014127
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French (fr)
Japanese (ja)
Inventor
Masao Umemoto
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Individual
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Individual
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Publication of WO2004044042A1 publication Critical patent/WO2004044042A1/en
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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/0026Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting
    • B29B17/0047Compacting complete waste articles
    • B29B17/0052Hollow articles, e.g. bottles
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J11/00Recovery or working-up of waste materials
    • C08J11/04Recovery or working-up of waste materials of polymers
    • C08J11/06Recovery or working-up of waste materials of polymers without chemical reactions
    • C08J11/08Recovery or working-up of waste materials of polymers without chemical reactions using selective solvents for polymer components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/0026Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting
    • B29B17/0047Compacting complete waste articles
    • B29B17/0052Hollow articles, e.g. bottles
    • B29B2017/0068Softening the hollow articles by heat and causing permanent deformation
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Definitions

  • Waste material recovery method waste material recovery equipment, volume reducing or softening liquid, waste material recovery system, recycling method and waste material separation and recovery method
  • the present invention relates to a method for collecting waste plastic materials such as plastic containers and bottles such as styrofoam, polyurethane foam, and polypropylene, a waste material recovery apparatus, a volume reduction or softening liquid, and a waste material recovery system. It relates to recycling methods and methods for separating and collecting waste materials.
  • waste plastic materials such as plastic containers and bottles such as styrofoam, polyurethane foam, and polypropylene
  • a waste material recovery apparatus such as styrofoam, polyurethane foam, and polypropylene
  • a waste material recovery apparatus such as styrofoam, polyurethane foam, and polypropylene
  • a waste material recovery apparatus such as styrofoam, polyurethane foam, and polypropylene
  • the direct heat reduction method has disadvantages such as generation of styrene monomer due to thermal decomposition, difficulty in uniform reduction and blackening of some parts, and complicated equipment. 1 — 2 3 2 3 2 7, Japanese Patent Application Laid-Open No. 2002-224 1 5 3 6) are receiving attention.
  • conventional solution reduction methods are harmful because they all use petroleum-based solvents (for example, even if oil extracted from food is used, those oils are harmful to the human body due to their high concentration) There is a serious danger that the risk of flammable explosion is high and that it takes a lot of cost to remove the solution from the reduced styrene.
  • volume reduction High human safety and environmental safety, and can reduce or reduce the volume of foaming materials such as styrene foam and polyethylene foam (hereinafter referred to as volume reduction), and plastics such as polyethylene, polypropylene, vinyl chloride, and polyester.
  • volume reduction foaming materials
  • plastics such as polyethylene, polypropylene, vinyl chloride, and polyester.
  • the container includes a bottle.
  • a solution or B solution includes the mixture of A and B. That is, it means “A solution or B solution or a mixture thereof”.
  • the waste material referred to in the present invention is not limited to a material to be disposed of and a material that has already been disposed of, but is a product that is in the middle of temporary storage, but is a product that is no longer a product and that requires volume reduction. In short, it includes all items that need to be reduced in volume. Disclosure of the invention
  • a solution of a diol or a polyol or a mixture thereof is heated to a predetermined temperature, and a foamed material, a plastic container or a plastic material is brought into contact with the heated solution to reduce the volume or to reduce the volume. Softening and collecting the foam, plastic container or plastic material simultaneously or later.
  • the method for recovering waste material comprises: contacting a diol or polyol solution or a mixture thereof with a foaming material, a plastic container, or a plastic material, or heating the solution while contacting the solution.
  • a method for recovering waste materials by reducing or softening the volume and collecting the foamed material, plastic container or plastic material simultaneously or later. Pressure is applied at the time of the contact or immediately after the contact.
  • the solution temperature is heated to a temperature in the range from 80 ° C. or higher to the boiling point.
  • the foamed material is foamed polystyrene or foamed polyethylene
  • the plastic container is a container made of polyethylene, polypropylene, or polyvinyl chloride, or a pet bottle, and the plastic material is polychlorinated.
  • Examples include vinyl, polyethylene, polypropylene, or polyester plates, tubes, sheets, nonwoven fabrics, cloths, and fiber bundles.
  • the solution temperature is a temperature within a range from 130 ° C. or higher to a boiling point
  • the waste material is a styrene foam, a pet bottle, or a container made of polyethylene.
  • the plastic material is a chip obtained by crushing or chopping a pet pot.
  • the foam material is foamed polyurethane, and the solution temperature is from 150 ° C. or higher to the boiling point. Up to.
  • the solution is diol or triol which is a raw material of polyurethane.
  • the diol is glycols or monoacylglycerol.
  • the dalicols are alkylenedaricols or a polymer thereof.
  • the alkylene glycols are diethylene dali glycol, trimethylene glycol, triethylene glycol, tetraethylene glycol cornole, butylene glycol cornole, dipropylene glycol, or propylene glycol.
  • the polymer is polyethylene glycol or polypropylene glycol, and the polyol is triol.
  • the triol is glycerin or trimethylolpropane.
  • the waste material is a pet bottle or a chip obtained by crushing or chopping a pet bottle, and the solution is ethylene glycol.
  • the waste material recovery device includes: a heating device that heats the diol or polyol to a predetermined temperature; and bringing the heated solution into contact with a foam material, a plastic container, or a plastic material; It is provided with a softening means for reducing the volume by spraying and softening, and a collecting means for collecting the foamed material, the plastic container, or the plastic material.
  • the apparatus further includes a pressurizer for applying pressure to the foam material, the plastic container, or the plastic material.
  • the heating device is configured by one or a combination of an induction heating device, a microwave heating device, an ultrasonic heating device, a high frequency vibration heating device, and an ultrasonic vibration heating device.
  • the waste material is a bottle, and there is a means for selecting one from the aggregate, and then the heated liquid comes into contact with the waste material by natural fall, spraying, spraying, etc. from the bottom of the press.
  • At least both the mouth and the bottom of the pet bottle are equipped with a structure that applies compressive force.
  • the volume reducing or softening liquid of the foamed material, plastic material, or plastic container according to the present invention is composed of a diol or polyol solution or a mixture thereof, and is heated at 80 to 200 ° C. or lower.
  • the volume-reducing or softening solution of the styrofoam or polyethylene product according to the present invention consists of a diol or polyol solution or a mixture thereof, and is heated to 130 ° C or more and 200 ° C or less. .
  • the volume reducing or softening liquid of the foamed polyurethane according to the present invention is a diol or a triol as a raw material of the polyurethane, and is heated to 150 ° C. or more and 230 ° C. or less.
  • the volume reducing or softening liquid of the pot pottle or the chip according to the present invention is ethylene daryl, which is heated to 80 ° C. or more and 190 ° C. or less.
  • the collection price is determined according to the weight of the waste plastic member recovered by the waste material recovery method.
  • the styrofoam collected by the method for collecting waste materials is washed with water or dried as necessary, and a styrene product is obtained by a reduced-pressure molding machine.
  • a diol or a polyol and a waste material are mixed, and the mixture is separated into one at the liquid surface and one that sinks in the liquid or at the bottom, and then recovers each.
  • FIG. 1 is a schematic view of a volume reduction / softening apparatus according to the present invention.
  • FIG. 2 is a schematic diagram of another volume reducing / softening apparatus according to the present invention.
  • FIG. 3 (a) is a schematic view of still another volume reducing / softening apparatus according to the present invention.
  • FIG. 3 (b) is a schematic view of still another volume reducing / softening apparatus according to the present invention.
  • FIG. 4 is a schematic diagram of a collecting device for collecting with a belt conveyor according to the present invention.
  • the method for treating waste material according to the present invention comprises heating a diol or polyol which is a volume reducing / softening solution, and contacting the heating solution with a foamed material / plastic of a single product or an aggregate. It also consists of collecting or separating material that has been reduced or softened or is being reduced.
  • the solution may be heated while the object is immersed in the solution at room temperature while the solution is applied or sprayed.
  • microwave irradiation there are microwave irradiation, ultrasonic irradiation and the like.
  • the pressure is preferably applied while in contact with the solution, but compression is possible even after contact if only a short time has elapsed.
  • the urethane foam softened by contact with the heating liquid loses elasticity and loses restoring force, it is possible to compress the urine even after a lapse of time after the contact.
  • styrene foam can be reduced to about 30 times. This reduction rate can be reduced to 1/100 by applying pressure. By applying pressure, the time can be shortened, and by applying a larger pressure, the solution can be compressed and discharged, so that the amount of remaining liquid can be reduced. In addition, even a portion that cannot be compressed only by pressure alone, for example, a portion of a mouth of a pet bottle, can be crushed or reduced by using a heating solution and pressure together.
  • Foamed polyethylene and the like cannot be reduced in volume only by pressure.
  • the volume reduction rate is small even with the heated volume reduction solution of the present invention alone.
  • the volume can be reduced by using the heating volume reducing solution and pressure together.
  • foamed polyurethane requires the combined use of pressure and heating liquid.
  • collection only single waste materials are collected, but in the case of mixed waste materials, it is possible to separate them according to the specific gravity of the solution, the fluidity when softened, the shape, etc. Collection can be performed at the time of volume reduction as well as after volume reduction. Finally, it is common practice to remove and dry the solution with water.
  • the diols or polyols used in the present invention develop volume-softening power only when heated and have no effect at room temperature.
  • the experiment in the case of styrofoam, only slight bubbles were generated on the surface at a liquid temperature of approximately 80 ° C, but bubbles slowly formed at 100 ° C, and bubbles were generated at 110 ° C. The onset was accelerated, and the volume decreased when the temperature exceeded 120 ° C, and at 130 ° C or more, the volume was reduced in a few seconds if the fragment was broken.
  • the pet bottle softened at 80 ° C.
  • High-pressure polyethylene softened above 105 ° C.
  • the liquid used in the present invention is a liquid, its boiling point is the upper limit.
  • the present invention includes heating to the boiling point to form steam, and applying it to waste material to rapidly reduce the volume.
  • Styrofoam, PET bottles, and polyethylene containers, plates, tubes, sheets, non-woven fabrics, cloths, etc. can be reduced in volume and softened without pressure by applying a temperature of 130 ° C or higher. is there.
  • PET bottles can greatly reduce transportation and storage costs by reducing the volume of bottles.
  • the collected PET bottles are finally collected as chips by crushing and shredding, stored, and transported to the next destination. Therefore, it is desired to further reduce the chip size, but at present, the technology has not been developed.
  • the volume of the chip can be further reduced. That is, the chip has a length of about several mm to 2 cm, but by attaching it to a liquid heated to, for example, 130 to 170 in the present invention, it can be reduced to a fraction. Can be reduced in volume. In the experiments, the volume reduction rate was larger for the aggregate of small chips. This is due to the warpage of large chips. It is only necessary to pour the heating liquid into the chip assembly, and if the pressure is further increased, the volume can be greatly reduced.
  • diols and polyols used in the present invention. Since diols and polyols are water-soluble and are not compatible with plastics, they have the advantage that they can be easily removed from plastic by washing with water, are highly safe, and do not require wastewater treatment of the washing liquid.
  • diols and polyols have high boiling points, and if they are used, most plastic materials will be subject to volume reduction and softening.
  • diols and polyols generally have a high flash point, but the risk of ignition and explosion or fire is hardly at the temperature according to the present invention (most of them are Class 4 and 3 petroleums of the Fire Service Law). is there.
  • the softened plastic material and the reduced foam material need to be centrifuged and strongly squeezed out with strong polar solutions such as diols and polyols by washing with water or applying pressure. is there. As a result, a plastic material / bottle with a small amount of solution mixed therein and a reduced-sized foam material can be obtained.
  • foamed polyurethane is a thermosetting resin, it does not soften or shrink with a heated liquid. So far, no solution capable of reducing the volume and softening has been found. In addition, resilient, large-volume polyurethane foam is one of the most troublesome waste disposal challenges in the future.
  • foaming polyurethane can be reduced in volume by heating the diol or polyol of the present invention to an appropriate temperature.
  • the temperature of the solution must be 150 ° C or higher, below which the volume will not decrease or it will take a long time.
  • the decomposition of foamed polyurethane proceeds at a high temperature of 200 ° C or more in many solutions. Decomposition is slight in short time even at 200 ° C or higher, but when time-sensitive work is difficult, 150 ° C to 200 ° C (glycerol and polyalkylene glycol are Up to 230 ° C). Even if short-time work is possible, the upper limit is 230 ° C.
  • soft urethane foam shrinks without decomposing when diethylene glycol is heated around 160 ° C and then immersed in it and applies compressive force. This phenomenon is called compression.
  • Diethylene glycol heated to 180 ° C reduced the volume to a fraction of that of a slightly harder, more resilient urethane foam when used together with pressure. mm).
  • compression of propylene glycol occurred at about 180 ° C, but at the same time, decomposition took place in a very short time.
  • Triethylene glycol was easily compressed when heated to around 180 ° C, but decomposed slightly. However, complete decomposition required a long time and a higher temperature.
  • the pressure is preferably applied while in contact with the solution, but compression is possible even after contact if only a short time has elapsed.
  • foamed polyurethane softened by contact with the heating liquid loses its elasticity and loses its restoring force, so that it can be compressed even after the elapse of time after contact.
  • a mixed solution of diol and polyalkylene glycol such as polyethylene glycol or polypropylene glycol having a molecular weight of 200 or more. Is preferably as high as 180 ° C. to 200 ° C.
  • a solution of a mixture of diethylene glycol and a half amount of polyethylene glycol (molecular weight: 200) showed little decomposition when heated to 180 ° C.
  • glycerol which is a triol, also has a weak contracting power, so it is desirable to use it as a liquid mixture with diol for the purpose of weakening the decomposition power.
  • diethylene glycol or triethylene daryl For highly resilient urethane foam, use diethylene glycol or triethylene daryl to select the optimal temperature between 170 ° C and 200 ° C depending on the urethane material, and press it. preferable.
  • diols such as hexanediol and triol
  • polyurethane There is no problem even if the decomposition of the tin proceeds slightly when the tin is brought into contact with the hot solution. This is because the decomposed product is daricol as a raw material, and the volume-reduced solution containing the decomposed product can be used for regeneration of polyethylene. Therefore, when these diols and triols are used, the present invention can be said to be an epoch-making volume reduction method.
  • the diol used in the present invention is defined as a compound having two alcoholic O H groups
  • the polyol is defined as a compound having three or more O H groups.
  • Diols include glycols and monoacylglycerols.
  • Glycols are alkylene groups such as a methylene group, an ethylene group, a propylene group, and a butylene group with two OH groups.
  • ethylene glycol and its 2, 3, and 4 Diethylene glycol, triethylene glycol, tetraethylene glycol, and the like, propylene glycol and its dimer and trimer dipropylene glycol, tripropylene glycol, etc., and other butyl groups
  • Ethylene glycol is highly toxic and unsuitable, so if it is used, it must be a closed system.
  • diethylene glycol (boiling point: 244 ° C), trimethylene glycol (2144 ° C), triethylene glycol (287 ° C), tetraethylene glycol (3 (27 ° C), butylene glycol (235 ° C), dipropylene glycol (232 ° C), and tripropylene glycol (268 ° C) are highly safe for humans. Since it has a high flash point and is difficult to burn, it is suitable as the solution of the present invention. In addition, the boiling points of these solutions are high, and most plastic materials can be softened.
  • high molecular weight alkylene glycols which are polymers of dalicols included in the diol, also have a reduced volume when heated.
  • polyethylene glycol, polypropylene glycol, etc. also reduce the size of the foam / plastic container and soften the plastic material. They are superior to other giols and triols in that they are less volatile at high temperatures.
  • Polypropylene glycol is a liquid, but polyethylene glycol with a molecular weight of 1000 or more is a solid at room temperature. The following are preferred in terms of handling.
  • triol is also useful for volume reduction.
  • Triols include glycerin, trimethylol ethane, trimethylolone propane, sonolevi tonole, mannitol, and other triols. These are solids, but become liquids when mixed with the other liquids of the present invention and heated.
  • Trimethylolpropane has a melting point of 59 ° C, easily turns into a liquid by heating, and has a boiling point of 292 ° C, which makes it difficult to volatilize, further reducing human and environmental safety. There are advantages such as high. Glycerin is also highly safe for humans, has an extremely high flash point, and has low flammability.
  • ethylene dalicol is used for the bottle and the liquid for reducing the volume of the chip, washing can be eliminated. Since ethylene glycol is a raw material for pet bottles, the volume-reduced liquid after use can be incorporated into the recycling process for disassembling pet bottles.
  • the apparatus for treating waste material of the present invention first requires an apparatus for heating the volume reducing solution to a predetermined temperature.
  • a system for applying a liquid that is, a method of applying a liquid, that is, a method of sprinkling, flowing in a shower shape, or a method of allowing the liquid to fall naturally
  • the heating device may be installed immediately before the liquid outlet.
  • the spraying method that is, the method of spraying or spraying the liquid together with the high-pressure air may be provided immediately before the liquid outlet. If not immediately before, the pipe to the heating section and the outlet is preferably insulated so that heat does not escape.
  • the tank When a large tank is filled with a solution and waste material is put into the tank to heat the liquid in the tank, the tank can be heated directly or the tank and heating section can be circulated separately. In the tank type, either the waste material is immersed in a heated solution or the solution is heated after immersion.
  • the recovery device can be applied to various kinds of waste materials, and therefore, a device capable of further applying pressure is required.
  • the pressure is generally a compressive force, and includes a piston method, a press method, and the like. It is efficient to apply the compressive force while immersing the volume-reduced material in the heating liquid or applying the heating liquid. However, the pressure may be immediately after removal from the soaked solution, immediately after applying the heating solution, or immediately after stopping the solution.
  • the reduced volume waste is collected.
  • the solution is sprinkled from above to reduce the dissolution, it is moved on a belt conveyor and placed in a collection box.
  • a net basket is submerged in the tank, which is raised and collected in a basket.
  • the solutions of the present invention are all high-frequency induction heating, micro wave heating, Rapid heating is possible by ultrasonic heating, high frequency vibration heating, ultrasonic vibration heating, etc. Infrared heating and far infrared heating are also possible.
  • high-frequency vibration heating and ultrasonic vibration heating are preferable because the equipment becomes compact and there is no danger of fire.
  • the ultrasonic heating means irradiating an ultrasonic wave of 16,000 Hz or more, but heating can be performed by high frequency vibration of several thousand Hz depending on irradiation time and intensity.
  • Microwave heating, ultrasonic heating, and ultrasonic vibration heating have the advantage that the equipment is compact because there is no heat source and there is no danger of fire.
  • the compaction of equipment using ultrasonic waves is particularly remarkable in systems in which liquid is sprinkled, sprayed, or sprayed. The reason is that the liquid temperature rises instantly if the ultrasonic wave is applied locally, so in these methods, it is sufficient to irradiate just before the nozzle, and the heating unit becomes compact.
  • the volume reduction tank 4 is divided into upper and lower parts, and there is a tank containing the volume reduction liquid 1 heated through a heater 8 at the upper part. 9 and pressurize it with a press 10 from above to reduce the volume while submerging the waste material in the liquid and sandwiching it between the flat nets 2.
  • open valve 5 After reducing the volume, open valve 5 and drop the liquid into waste tank 3 at the bottom of the tank.
  • the press again descends and squeezes the solution.
  • the press is lifted up, then the net is also lifted up and the waste is collected.
  • the heated liquid is poured into the tank from above the injection port 7, and new waste is put into the tank first. First, waste material is put into the tank, and then the liquid heated from above is sprayed from the injection port.
  • the potters 16 are placed side by side, and pressurized from above while adding a heating liquid from the pores 14 to constrict.
  • This method of laying the bottle on its side and compressing the entire body makes it difficult for the solution to enter the bottle and there is no need to align the bottle.
  • the volume reducing solution in the solution tank 18 is sent upward by the air compressor 19, heated by the ultrasonic heater 11, and injected into the space in the compressor.
  • the compression surface 13 is lowered, and the softened bottle is compressed downward.
  • the waste liquid from the drain 15 may be returned to the tank 18.
  • the compressor is lowered so that the pet bottle is sent by the belt conveyor and only the mouth and bottom of the pet bottle are crushed at the same time.
  • the heated solution 21 is sprinkled from the hole on the bottom of the compressor.
  • an ultrasonic heater 11 is provided immediately before the liquid is injected into the compression plate 10.
  • the middle part of the bottle shrinks only by the application of the solution, even if no pressure is applied, so that it comes into contact with the heated solution, and if pressure is applied, the mouth and bottom are also pressed. Can be flattened. At this time, since the middle part shrinks, a greater volume reduction rate can be obtained than with pressure alone.
  • the bottom surface may be flat as shown in Fig. 3 (b). This can be applied to styrofoam.
  • the foamed material and the plastic material are placed in the container containing the solution without distinction, and the heated solution is sprayed on them, Sorting based on weight, fluidity, and size allows for separate collection naturally.
  • the plastics 9 except petroleum chloride and polyester are diols It can be collected by pulling it up diagonally upward on conveyor 25 as it is in contact with the surface of the building by buoyancy.
  • Collection equipment will be installed at supermarkets, convenience stores, or municipal collection points. Waste plastic materials collected from these collection sites are collected by municipalities and waste disposal companies. At this time, the pickup price is determined according to the weight. Therefore, according to the present invention, a large amount of waste plastic can be transported at one time because the degree of reduction of the waste plastic material is large, and therefore, more profits can be obtained for the carrier in one recovery.
  • the reduced volume of styrofoam obtained by the method of the present invention is obtained by removing the attached liquid by washing with water, and then drying it to obtain a pellet of an appropriate size (at the stage of styrofoam, If the volume is reduced to an appropriate size, it is possible that each pellet will have an appropriate pellet at the time of volume reduction), and it will be possible to obtain polystyrene again by using an extrusion molding machine under reduced pressure. it can. If the temperature of the volume-reducing liquid does not exceed 200 ° C, thermal denaturation is unlikely to occur, and polystyrene with good physical properties is regenerated.
  • a plastic reduced in volume according to the present invention or a plastic before volume reduction is mixed in a diol or a polyol
  • a container, a plate, a sheet, a nonwoven fabric, or the like such as styrene foam and polyethylene or polypropylene floats on the liquid surface.
  • Pet bottles, polyester or PVC plates, sheets, etc. which are destroyed and filled with solution, sink to the bottom. Therefore, first, a force for scooping styrofoam, polyethylene, polypropylene and the like is poured out and taken out, and then polyester and bichloride are taken out, and these can be separated.
  • the temperature of the softening and volume reducing solution (each of which may be mixed with a reducing solution to give characteristics) is set to about 130 to 200 ° C. Is good. This temperature increases the processing speed and increases the amount of plastics 4 That's why.
  • put a container such as a piece of foam material or plastic material, or a bottle in the same container or in a separate container, and stir or push the fragment into the solution to make sufficient contact with the liquid. .
  • applying pressure can speed up the volume reduction. Applying strong pressure can increase the volume reduction rate and further increase the processing speed.
  • the volume-reducing softening liquid does not need to be used alone, and may be used as a mixture in consideration of flammability, fluidity, boiling point, difficulty of heating, target plastic, and the like.
  • thermosetting resin most plastics other than the thermosetting resin can be reduced in volume or softened by increasing the temperature and combining the compressive force. If limited to polystyrene foam, water bottles, polyethylene containers, etc., the volume can be reduced or softened even at a relatively low temperature.
  • PET bottles can be used as a raw material for polyester to reduce the volume of foamed polyurethane, and the reduced volume at that time can be used as a raw material for polyurethane.
  • the collection price is determined according to the weight of the waste plastic material collected by the above-mentioned collection device.
  • waste plastic members such as foam materials, plastic containers, pet bottles, or plastic materials are collected, and the volume is reduced or softened as described above. Remanufactured products are made from the recycled blasting materials.
  • Extrusion molding using a waste plastic member such as a foam material, plastic container, plastic bottle, or plastic material treated by the above-mentioned volume reduction or softening method and the above-mentioned recovery device and equipped with a decompression device in a cylinder It is molded by a press or an injection molding machine.
  • Propylene grease 100 m1 was heated by microwave in a microwave oven (500 W) for 2 minutes. At that time, the liquid temperature was 120. The styrofoam fragments were put into it, and they were pushed into the solution with a stick and pressure was applied.
  • the mixture was heated in a microwave oven using 100 ml of Glyceronore, and cooled to a liquid temperature of 125 to 150. The volume was reduced to the same nucleus as in Example 1.
  • Polyethylene glycol (molecular weight: 400) 100 m1 is heated in a microwave oven
  • the temperature was set to 170 ° C, and a small piece of styrofoam was put therein, and the volume was reduced instantaneously.
  • Soft foamed polyurethane in diethylene glycol (170 ° C) heated electrically 6 and left for 5 minutes to soften. Next, the liquid was transferred to another container and pressed from above to reduce the volume of the flexible urethane foam. Also, 10 g of polypropylene was softened.
  • a mixture of 1 O ml of diethylene glycol and 1 O ml of triethylene glycol was heated to 18 in a microwave oven, and the foamed polyurethane was softened by pouring it for about 1 minute, then removed, and the absorbent was pressed down and removed. . This one did not reappear, and the volume was reduced.
  • Polyethylene dalicol (molecular weight: 600) is placed in a 50 O ml beaker, the liquid temperature is set to 160 ° C, and a hard PET bottle for carbonated drinks is set up in the beaker. Allowed.
  • Diethylene glycol was placed in a beaker, heated in a microwave oven (500 W) to about 170 ° C., and about 10 cm 3 of foamed polyurethane was put therein. After swelling for a while, it softened in a few minutes, so it was taken out, placed on water-absorbent paper and pressed from above to reduce the volume, and did not swell again.
  • Example 14 Add 20 ml of tetraethylene glycol to 20 ml of diethylene glycol, mix, and heat to 180 ° C in a microwave oven. There, about 10 cm 3 of foamed polyurethane was put. As in Example 14, softening was performed in 1 to 2 minutes, and the volume was reduced by pressing.
  • Tetraethylene dalicol was heated to 180, and the foamed polyurethane was softened in the same manner and reduced by applying pressure.
  • Tetraethylene glycol was heated to 170 ° C, and the carbonated beverage pot was laid sideways, and the heated liquid was poured from above and compressed by applying pressure from above on a melamine plate.
  • the mouth and bottom of the PET bottle are extremely hard and cannot be crushed by pressure alone. However, while the liquid at 170 ° C was applied, the mouth and bottom could be crushed simply by pressing with human hands from above.
  • a pet bottle with a diameter of 7 cm, a length of 21 cm, and a mouth diameter of 3 cm was reduced to a flat plate having a thickness of 1 cm and a length of 13 cm. This volume reduction rate is superior to any other volume reduction method.
  • the most suitable objects for the present invention are styrofoam and polyethylene foam in the case of foam materials.
  • it can be applied to pet bottles, polyethylene containers, polypropylene containers, and PVC containers.
  • plastics such as polyethylene, PVC, polypropylene, and polyester plates, tubes, sheets, nonwoven fabrics, cloths, and fiber bundles.
  • the system can be applied to a recycling system that collects waste plastic materials such as foam materials, plastic containers, pet bottles, and plastic materials, and uses recycled plastic materials as raw materials to produce products. These are the most in demand in modern society.

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Abstract

A collecting apparatus for foam materials, plastic containers, and plastic materials, wherein diol or polyol liquid is heated from the temperature of 80°C to the boiling point thereof, the foam materials, plastic containers, and plastic materials are immersed in the liquid, or the liquid is spattered or sprayed over these materials and containers and, as necessary, a pressure is applied thereto to reduce the volume or soften the foam materials, plastic containers, and plastic materials, and then the reduced or softened materials and containers are collected.

Description

明細書 廃材の回収方法、 廃材の回収装置、 減容液又は軟化液、 廃材の回収システム、 リサイクル方法及び廃材の分別回収方法 技術分野  Description Waste material recovery method, waste material recovery equipment, volume reducing or softening liquid, waste material recovery system, recycling method and waste material separation and recovery method

本発明は、 発泡スチロール、 発泡ポリ ウレタン、 ポリプロピレン等のプラスチ ック容器ゃぺッ トボトル等の廃プラスチック材の廃材の回収方法、 廃材の回収装 置、 減容液又は軟化液、 廃材の回収システム、 リサイクル方法及ぴ廃材の分別回 収方法に関する。 背景技術  The present invention relates to a method for collecting waste plastic materials such as plastic containers and bottles such as styrofoam, polyurethane foam, and polypropylene, a waste material recovery apparatus, a volume reduction or softening liquid, and a waste material recovery system. It relates to recycling methods and methods for separating and collecting waste materials. Background art

発泡スチロールの発泡材の縮小法と しては、 直接加熱縮小法、 溶媒縮小法の 2 種類がある。 直接加熱縮小法では、 熱分解によ りスチレンモノマーが発生する、 均一縮小が困難で一部黒化する、 装置が複雑になる、 などの欠点があり、 溶液縮 小法 (特開 2 0 0 1 — 2 3 2 3 2 7、 特開 2 0 0 2— 2 4 1 5 3 6など) が着目 をあびている。 しかし、 従来の溶液縮小法は、 すべて石油系溶剤を用いており有 害 (例えば、 食物からの抽出油を用いるものであっても、 それらのオイルは高濃 度のため人体に有害である) であり、 引火爆発の危険性が高く、 かつ、 縮小スチ ロールから溶液を除くのに多大なコス トがかかるなど致命的な欠点がある。 又、 ポリエチレン等のプラスチック材を軟化するには、 現在のところ加熱による方法 しかなく、 熱変性のため再生利用が難しい。 さらに、 発泡ポリ ウレタンは熱縮小 も難しく、 現在のところ高温焼却しか方法がなく有用なリサイクル方法の開発が 求められている。  There are two methods for reducing the foamed material of Styrofoam: the direct heat reduction method and the solvent reduction method. The direct heat reduction method has disadvantages such as generation of styrene monomer due to thermal decomposition, difficulty in uniform reduction and blackening of some parts, and complicated equipment. 1 — 2 3 2 3 2 7, Japanese Patent Application Laid-Open No. 2002-224 1 5 3 6) are receiving attention. However, conventional solution reduction methods are harmful because they all use petroleum-based solvents (for example, even if oil extracted from food is used, those oils are harmful to the human body due to their high concentration) There is a serious danger that the risk of flammable explosion is high and that it takes a lot of cost to remove the solution from the reduced styrene. At present, the only way to soften plastic materials such as polyethylene is by heating, which is difficult to recycle due to thermal denaturation. Furthermore, it is difficult to reduce the heat of foamed polyurethane. At present, there is no other method than high-temperature incineration, and there is a need to develop a useful recycling method.

人体安全性及ぴ環境安全性が高く、 発泡スチロール、 発泡ポ リ エチレン等の発 泡材を減容又は縮小 (以下、 減容という) でき、 ポリ エチレン、 ポリ プロ ピレン 、 塩化ビュル、 ポリエステル等のプラスチックを軟化できる画期的溶液を見出す 。 又、 廃材と して現在最も問題が生じている発泡ポリ ウレタンの減容液を見出す 。 次に、 この溶液を用いた減容 · 軟化のためのシステムを考え出す。 High human safety and environmental safety, and can reduce or reduce the volume of foaming materials such as styrene foam and polyethylene foam (hereinafter referred to as volume reduction), and plastics such as polyethylene, polypropylene, vinyl chloride, and polyester. Find a breakthrough solution that can soften. In addition, find a volume reduction solution of foamed polyurethane that is currently causing the most problems as waste materials. . Next, a system for volume reduction and softening using this solution is devised.

なお、 本発明では、 容器にはボトルも含まれる。 " A溶液又は B溶液" は Aと Bの混合も含める。 すなわち、 " A溶液又は B溶液もしく はそれらの混合液" を 意味する。 本発明でいう廃材とは廃棄予定物と、 既に廃棄された物に限定されず 、 一時保管の中間の製品であるが、 製品にならなく なった物で、 減容の必要が生 じた物など、 要は減容の必要が生じた物全てを含む。 発明の開示  In the present invention, the container includes a bottle. "A solution or B solution" includes the mixture of A and B. That is, it means "A solution or B solution or a mixture thereof". The waste material referred to in the present invention is not limited to a material to be disposed of and a material that has already been disposed of, but is a product that is in the middle of temporary storage, but is a product that is no longer a product and that requires volume reduction. In short, it includes all items that need to be reduced in volume. Disclosure of the invention

本発明に係る廃材の回収方法は、 ジオール又はポリオールの溶液もしく はそれ らの混合液を所定の温度に加熱し、 該加熱溶液に発泡材、 プラスチック容器又は プラスチック材を接触させて減容又は軟化させ、 同時に又は後で該発泡材、 ブラ スチック容器又はプラスチック材を収集してなる。  In the method for collecting waste materials according to the present invention, a solution of a diol or a polyol or a mixture thereof is heated to a predetermined temperature, and a foamed material, a plastic container or a plastic material is brought into contact with the heated solution to reduce the volume or to reduce the volume. Softening and collecting the foam, plastic container or plastic material simultaneously or later.

本発明に係る廃材の回収方法は、 ジオール又はポリオールの溶液もしく はそれ らの混合液と発泡材、 プラスチック容器又はプラスチック材を接触させた状態で 、 もしく は接触させながら溶液を加熱して減容又は軟化させ、 同時に又は後で該 発泡材、 プラスチック容器又はプラスチック材を収集してなる廃材の回収方法。 前記接触時に又は接触直後に圧力を加える。  The method for recovering waste material according to the present invention comprises: contacting a diol or polyol solution or a mixture thereof with a foaming material, a plastic container, or a plastic material, or heating the solution while contacting the solution. A method for recovering waste materials by reducing or softening the volume and collecting the foamed material, plastic container or plastic material simultaneously or later. Pressure is applied at the time of the contact or immediately after the contact.

前記溶液温度を 8 0 °C以上から沸点までの範囲内の温度に加熱する。  The solution temperature is heated to a temperature in the range from 80 ° C. or higher to the boiling point.

前記発泡材は、 発泡スチロール又は発泡ポリ エチレンであり、 前記プラスチッ ク容器は、 ポリエチレン製、 ポリプロピレン製、 又はポリ塩化ビニル製の容器、 もしく はぺッ トポ トルであり、 前記プラスチック材は、 ポリ塩化ビニル製、 ポリ エチレン製、 ポ リ プロ ピレン製、 又はポ リ エステル製の板、 筒状、 シー ト、 不織 布、 布、 繊維束等である。  The foamed material is foamed polystyrene or foamed polyethylene, and the plastic container is a container made of polyethylene, polypropylene, or polyvinyl chloride, or a pet bottle, and the plastic material is polychlorinated. Examples include vinyl, polyethylene, polypropylene, or polyester plates, tubes, sheets, nonwoven fabrics, cloths, and fiber bundles.

前記溶液温度が 1 3 0 °C以上から沸点までの範囲内の温度であり、 前記廃材が 発泡スチロール、 ぺッ トボトル又はポリエチレン製の容器である。  The solution temperature is a temperature within a range from 130 ° C. or higher to a boiling point, and the waste material is a styrene foam, a pet bottle, or a container made of polyethylene.

前記プラスチック材が、 ぺッ トポトルを粉砕又は細断して得られるチップであ る。  The plastic material is a chip obtained by crushing or chopping a pet pot.

前記発泡材が発泡ポリ ウレタンであり、 前記溶液温度が 1 5 0 °C以上から沸点 までである。 The foam material is foamed polyurethane, and the solution temperature is from 150 ° C. or higher to the boiling point. Up to.

前記溶液が、 ポリ ウレタンの原料であるジオール又はト リオールである。  The solution is diol or triol which is a raw material of polyurethane.

前記ジオールがグリ コール類又はモノァシルグリセ口ールである。  The diol is glycols or monoacylglycerol.

前記ダリ コール類がアルキレンダリ コール類又はその重合体である。  The dalicols are alkylenedaricols or a polymer thereof.

前記アルキレングリ コール類がジエチレンダリ コール、 ト リメチレングリ コー ル、 ト リ エチレングリ コール、 テ トラエチレングリ コーノレ、 ブチレングリ コーノレ 、 ジプロ ピレングリ コール、 又は ト リ プロ ピレングリ コールである。  The alkylene glycols are diethylene dali glycol, trimethylene glycol, triethylene glycol, tetraethylene glycol cornole, butylene glycol cornole, dipropylene glycol, or propylene glycol.

前記重合体が、 ポリエチレングリ コール又はポリプロ ピレングリ コールである 前記ポリオールが トリオールである。  The polymer is polyethylene glycol or polypropylene glycol, and the polyol is triol.

前記ト リオールがグリセリ ン、 又はト リメチロールプロパンである。  The triol is glycerin or trimethylolpropane.

前記廃材がぺッ トボ トル又はぺッ トボ トルを破砕又は細断して得られるチッ プであり、 前記溶液がエチレングリ コールである。  The waste material is a pet bottle or a chip obtained by crushing or chopping a pet bottle, and the solution is ethylene glycol.

本発明に係る廃材の回収装置は、 前記ジオール又はポリオールを所定の温度に 加熱する加熱装置と、 該加熱された溶液と発泡材、 プラスチック容器、 又はブラ スチック材とを接触させる、 浸す、 かける、 吹き付けて減容 · 軟化させるための 減容 ' 軟化手段と、 該発泡材、 プラスチック容器、 又はプラスチック材を収集す る収集手段とを備える。  The waste material recovery device according to the present invention includes: a heating device that heats the diol or polyol to a predetermined temperature; and bringing the heated solution into contact with a foam material, a plastic container, or a plastic material; It is provided with a softening means for reducing the volume by spraying and softening, and a collecting means for collecting the foamed material, the plastic container, or the plastic material.

前記発泡材、 プラスチック容器、 又はプラスチック材に圧力を加えるための加 圧機をさらに備える。  The apparatus further includes a pressurizer for applying pressure to the foam material, the plastic container, or the plastic material.

前記加熱装置は、 誘導加熱装置、 マイクロ波加熱装置、 超音波加熱装置、 高周 波振動加熱装置、 又は超音波振動加熱装置のいずれか 1つ又は組み合わせて構成 される。  The heating device is configured by one or a combination of an induction heating device, a microwave heating device, an ultrasonic heating device, a high frequency vibration heating device, and an ultrasonic vibration heating device.

前記廃材がぺッ トボトルであり、 その集合体より 1つが選別される手段があり、 次に加温された液が加圧機底面よ り 自然落下、 吹きつけ、 スプレー等によ り廃材 と接触し、 ぺッ トボトルの少なく とも口部と底部の両方に圧縮力がかかる構造を 備える。  The waste material is a bottle, and there is a means for selecting one from the aggregate, and then the heated liquid comes into contact with the waste material by natural fall, spraying, spraying, etc. from the bottom of the press. At least both the mouth and the bottom of the pet bottle are equipped with a structure that applies compressive force.

タンクに減容液があり 、 該タンクに廃材を入れて減容し、 又は減容しつつある 廃材を浮力によつて液面に浮かせ、 減容した廃材を斜め上方に上昇するベルトに より掬い上げる構造を備える。 There is a volume reduction liquid in the tank, and waste is put into the tank to reduce the volume, or the volume is decreasing. Equipped with a structure in which waste material is floated on the liquid surface by buoyancy, and the reduced waste material is scooped up by a belt that rises diagonally upward.

本発明に係る発泡材、 プラスチック材、 又はプラスチック容器の減容又は軟化 液は、 ジオール又はポリオール溶液もしくはそれらの混合液からなり、 8 0で以 上 2 0 0 °C以下に加熱してなる。  The volume reducing or softening liquid of the foamed material, plastic material, or plastic container according to the present invention is composed of a diol or polyol solution or a mixture thereof, and is heated at 80 to 200 ° C. or lower.

本発明に係る発泡スチロール又はポリエチレン製品の減容又は軟化液は、 ジォ ール又はポリオール溶液もしく はそれらの混合液からなり、 1 3 0 °C以上 2 0 0 °C以下に加熱してなる。  The volume-reducing or softening solution of the styrofoam or polyethylene product according to the present invention consists of a diol or polyol solution or a mixture thereof, and is heated to 130 ° C or more and 200 ° C or less. .

本発明に係る発泡ポリ ウレタンの減容又は軟化液は、 ポリ ウレタンの原料とな るジオール又はト リオールであり、 1 5 0 °C以上 2 3 0 °C以下に加熱してなる。 本発明に係るぺッ トポトル又はそのチップの減容又は軟化液は、 エチレンダリ コールであり、 8 0 °C以上 1 9 0 °C以下に加熱してなる。  The volume reducing or softening liquid of the foamed polyurethane according to the present invention is a diol or a triol as a raw material of the polyurethane, and is heated to 150 ° C. or more and 230 ° C. or less. The volume reducing or softening liquid of the pot pottle or the chip according to the present invention is ethylene daryl, which is heated to 80 ° C. or more and 190 ° C. or less.

本発明に係る廃材の回収システムは、 廃材の回収方法により回収した廃プラス チック部材の重量に応じて引き取り価格が決められる。  In the waste material recovery system according to the present invention, the collection price is determined according to the weight of the waste plastic member recovered by the waste material recovery method.

本発明に係る発泡スチロールのリサイクル方法は、 廃材の回収方法により回収 した発泡スチロールを必要に応じて水洗し、 又は乾燥して、 減圧式の成形機によ りスチロール製品を得る。  In the method for recycling styrofoam according to the present invention, the styrofoam collected by the method for collecting waste materials is washed with water or dried as necessary, and a styrene product is obtained by a reduced-pressure molding machine.

本発明に係るプラスチックの廃材の分別回収方法は、 ジオール又はポリオール と廃材とを混合し、 液面にあるものと、 液中又は底に沈むものに分けた後、 それ ぞれを回収する。 図面の簡単な説明  In the method for separating and collecting plastic waste material according to the present invention, a diol or a polyol and a waste material are mixed, and the mixture is separated into one at the liquid surface and one that sinks in the liquid or at the bottom, and then recovers each. BRIEF DESCRIPTION OF THE FIGURES

第 1図は、 本発明の係る減容 · 軟化装置の概略図である。 FIG. 1 is a schematic view of a volume reduction / softening apparatus according to the present invention.

第 2図は、 本発明の係る他の減容 · 軟化装置の概略図である。 FIG. 2 is a schematic diagram of another volume reducing / softening apparatus according to the present invention.

第 3 ( a ) 図は、 本発明の係るさらに他の減容 · 軟化装置の概略図である。 FIG. 3 (a) is a schematic view of still another volume reducing / softening apparatus according to the present invention.

第 3 ( b ) 図は、 本発明の係るさらに他の減容 · 軟化装置の概略図である。 FIG. 3 (b) is a schematic view of still another volume reducing / softening apparatus according to the present invention.

図 4は、 本発明の係るベルトコンベアで収集する収集装置の概略図である。 発明を実施するための最良の形態 FIG. 4 is a schematic diagram of a collecting device for collecting with a belt conveyor according to the present invention. BEST MODE FOR CARRYING OUT THE INVENTION

本発明の廃材の処理方法は、 減容 · 軟化溶液であるジオール又はポリオールを 加熱すること、 単品又は集合体の発泡材ゃプラスチックに加熱溶液を接触するこ とからなる。 さらに減容又は軟化した物又はしつつある物を集め、 又は分別する ことからなる。 接触させる方式には、 溶液をためておき、 加温し、 そこへ、 対象 物を入れる場合と、 加温した溶液を対象物にかけたり、 吹きつけたりする場合と がある。 また、 対象物を室温の溶液に浸した状態で、 溶液をかけたり、 又は吹き 化つけながら、 溶液を加温してもよい。 溶液をかけたり、 又は吹きつけながら溶 液を加温する方法と しては、 マイクロ波照射、 超音波照射などがある。  The method for treating waste material according to the present invention comprises heating a diol or polyol which is a volume reducing / softening solution, and contacting the heating solution with a foamed material / plastic of a single product or an aggregate. It also consists of collecting or separating material that has been reduced or softened or is being reduced. There are two methods of contacting: storing the solution, heating it, and putting the object into it, or pouring or spraying the heated solution onto the object. Alternatively, the solution may be heated while the object is immersed in the solution at room temperature while the solution is applied or sprayed. As a method of heating the solution while applying or spraying the solution, there are microwave irradiation, ultrasonic irradiation and the like.

加温溶液と接触させる前に圧力のみによ りある程度圧縮しておき、 圧力を除去 した後に加温溶液と接触させる。 また、 加温溶液と接触させている時、 もしくは 、 接触させた直後に圧力を加える方法もある。 直後であれば熱により減溶 · 軟化 している間に、 圧力を加えることにより、 減容の速度を速く し、 かつ減容率を大 きくすることができる。  Before contact with the warming solution, compress it to some extent only with pressure, and after releasing the pressure, contact with the warming solution. There is also a method of applying pressure during or immediately after contact with the heating solution. Immediately after that, while the material is being melted and softened by heat, pressure can be applied to increase the volume reduction rate and increase the volume reduction rate.

圧力は、 溶液と接触している状態でかけるのが好ましいが、 接触後であっても 短時間しか経過していなければ圧縮は可能である。 但し、 加温液と接触させて軟 化した発泡ウレタンは、 弾力を失い復元力がなくなるので、 接触後時間が経た後 、 時間が経過しても圧縮することが可能である。  The pressure is preferably applied while in contact with the solution, but compression is possible even after contact if only a short time has elapsed. However, since the urethane foam softened by contact with the heating liquid loses elasticity and loses restoring force, it is possible to compress the urine even after a lapse of time after the contact.

本発明の加温溶液を使えば、 例えば発泡スチロールを、 約 3 0分の 1に縮小で きる。 この縮小率は、 圧力を加えることによ り、 数 1 0 0分の 1 にすることがで きる。 圧力を加えれば、 時間も短縮でき、 より大きな圧力を加えることにより溶 液を圧縮排出させることができるので、 残存する液の量を減らすことができる。 又、 単に圧力のみでは、 圧縮が不可能な部分、 例えばペッ トボトルの口の部分で あっても、 加温溶液と圧力との併用により、 潰し、 又は縮小できる。  By using the heating solution of the present invention, for example, styrene foam can be reduced to about 30 times. This reduction rate can be reduced to 1/100 by applying pressure. By applying pressure, the time can be shortened, and by applying a larger pressure, the solution can be compressed and discharged, so that the amount of remaining liquid can be reduced. In addition, even a portion that cannot be compressed only by pressure alone, for example, a portion of a mouth of a pet bottle, can be crushed or reduced by using a heating solution and pressure together.

発泡ポリエチレンなどは圧力のみでは減容は不可能である。 本発明の加温した 減容液のみでも減容率は小さい。 この場合、 加温減容液と圧力を併用することに より減容が可能となる。 又、 発泡ポリ ウレタンも、 圧力と加温液の併用が必要で ある。 収集では、 単一廃材の場合は集めるのみであるが、 混合廃材では、 溶液に対す る比重や、 軟化した場合の流動性、 形状等によって分別が可能である。 収集は、 減容後のみでなく減容時に行うことも可能である。 最後に、 一般的には、 溶液を 水洗して除去し乾燥することが行われる。 Foamed polyethylene and the like cannot be reduced in volume only by pressure. The volume reduction rate is small even with the heated volume reduction solution of the present invention alone. In this case, the volume can be reduced by using the heating volume reducing solution and pressure together. In addition, foamed polyurethane requires the combined use of pressure and heating liquid. In the case of collection, only single waste materials are collected, but in the case of mixed waste materials, it is possible to separate them according to the specific gravity of the solution, the fluidity when softened, the shape, etc. Collection can be performed at the time of volume reduction as well as after volume reduction. Finally, it is common practice to remove and dry the solution with water.

本発明で用いるジオール又はポリオールは、 加温することにより初めて減容 - 軟化力が発現し、 室温では全く効力はないことを注記しておかねばならない。 実験では、 発泡スチロールにおいては、 おおむね液温 8 0 °Cで表面にわずかな 気泡が発生したのみであるが、 1 0 0 °Cで気泡がゆるやかに発生し、 1 1 0 °Cで は気泡の発生は早まり、 1 2 0 °Cをこえると減容がおこり、 1 3 0 °C以上では断 片であれば数秒で減容した。  It should be noted that the diols or polyols used in the present invention develop volume-softening power only when heated and have no effect at room temperature. In the experiment, in the case of styrofoam, only slight bubbles were generated on the surface at a liquid temperature of approximately 80 ° C, but bubbles slowly formed at 100 ° C, and bubbles were generated at 110 ° C. The onset was accelerated, and the volume decreased when the temperature exceeded 120 ° C, and at 130 ° C or more, the volume was reduced in a few seconds if the fragment was broken.

ペッ トボトルは 8 0 °Cで軟化した。 高圧法ポリエチレンは 1 0 5 °C以上で軟化 した。 温度は高い程、 減容、 軟化の速度は大きくなる。 本発明で用いるのは液体 なので、 その沸点が上限となる。 沸点まで加熱して蒸気と し、 それを廃材にあて て急速減容させることも本発明に含める。 発泡スチロール、 ペッ トボトル、 及ぴ ポリエチレン製の容器、 板、 筒、 シート、 不織布、 布等については、 1 3 0 °C以 上とすることにより、 圧力をかけなく とも、 減容 · 軟化が可能である。  The pet bottle softened at 80 ° C. High-pressure polyethylene softened above 105 ° C. The higher the temperature, the greater the rate of volume reduction and softening. Since the liquid used in the present invention is a liquid, its boiling point is the upper limit. The present invention includes heating to the boiling point to form steam, and applying it to waste material to rapidly reduce the volume. Styrofoam, PET bottles, and polyethylene containers, plates, tubes, sheets, non-woven fabrics, cloths, etc. can be reduced in volume and softened without pressure by applying a temperature of 130 ° C or higher. is there.

ペッ トボトルは、 ボトルを減容することにより、 輸送や保管のコス トを大きく 減らせる。 集められたペッ トボトルは、 最後は、 破碎ゃ細断によりチップと して 集められて、 保管され、 次なる目的地に輸送される。 そこで、 チップをさらに減 容することが望まれているが、 現在では、 その技術は開発されていない。 本発明 によれば、 チップをさらに減容できる。 すなわち、 チップは数 m m〜 2 c m程度 の長さのものであるが、 これを、 本発明の例えば 1 3 0〜 1 7 0 に加温した液 体につけることによ り、 数分の一に減容できる。 実験では、 小さいチップの集合 体の方が減容率は大きくなつた。 これは、 大きなチップの場合、 そりが生じるた めである。 チップの集合体に、 加温液体を流し込むだけでも良く、 さらに圧力を 加えれば大きく減容が可能である。  PET bottles can greatly reduce transportation and storage costs by reducing the volume of bottles. The collected PET bottles are finally collected as chips by crushing and shredding, stored, and transported to the next destination. Therefore, it is desired to further reduce the chip size, but at present, the technology has not been developed. According to the present invention, the volume of the chip can be further reduced. That is, the chip has a length of about several mm to 2 cm, but by attaching it to a liquid heated to, for example, 130 to 170 in the present invention, it can be reduced to a fraction. Can be reduced in volume. In the experiments, the volume reduction rate was larger for the aggregate of small chips. This is due to the warpage of large chips. It is only necessary to pour the heating liquid into the chip assembly, and if the pressure is further increased, the volume can be greatly reduced.

この時、 加温液体を加えた後圧力を加えるのではなく、 チップの集合体に圧力 を加えておき、 その状態で加温液体をかけるようにすれば大きいチップでも減容 率を大きくすることができる。 なお圧力が加わっても、 ポリエチレンテレフタレ ートの融点以下であればチップどう しがく っつきあう ことはない。 At this time, instead of applying pressure after adding the heating liquid, pressure is applied to the chip assembly, and if the heating liquid is applied in that state, the volume of even a large chip can be reduced. The rate can be increased. Note that even if pressure is applied, the chips do not stick to each other if the melting point is lower than the melting point of polyethylene terephthalate.

ここで、 本発明で用いるジオール、 ポリオールの一般的性質とその効果につい て述べる。 ジオール、 ポリオールは水溶性であって、 プラスチックとなじまない ため、 水洗により容易にプラスチックから液を除く ことができる うえ、 安全性が 高く、 水洗液を廃水処理する必要がないという利点がある。  Here, general properties and effects of the diols and polyols used in the present invention will be described. Since diols and polyols are water-soluble and are not compatible with plastics, they have the advantage that they can be easily removed from plastic by washing with water, are highly safe, and do not require wastewater treatment of the washing liquid.

そして、 ジオール、 ポリオールには高沸点のものがあり、 それらを用いればほ とんどのプラスチック材が減容 ' 軟化の対象となる。  Also, some diols and polyols have high boiling points, and if they are used, most plastic materials will be subject to volume reduction and softening.

さらに着目すべきは、 一般にジオール、 ポリオールは引火点が高いが、 引火爆 発や火災の危険性は本発明の温度ではほとんどない (ほとんどが消防法第 4類第 3石油類である) ことである。  It should be further noted that diols and polyols generally have a high flash point, but the risk of ignition and explosion or fire is hardly at the temperature according to the present invention (most of them are Class 4 and 3 petroleums of the Fire Service Law). is there.

最後に、 軟化したプラスチック材、 及び縮小した発泡材は、 ジオールやポリオ ール等の強極性溶液に対して、 ぬれが悪いため遠心分離し、 水洗し又は圧力を加 えてしぼり出すことが必要である。 これにより、 溶液の混入の少ないプラスチッ ク材ゃボトル、 発泡材の縮小体が得られる。  Finally, the softened plastic material and the reduced foam material need to be centrifuged and strongly squeezed out with strong polar solutions such as diols and polyols by washing with water or applying pressure. is there. As a result, a plastic material / bottle with a small amount of solution mixed therein and a reduced-sized foam material can be obtained.

さて、 発泡ポリ ウレタンは熱硬化性樹脂であるため、 加温した液体で軟化又は 縮小することはない。 これまで減容 · 軟化させうる溶液が見出されていない。 さ らに、 弾力があり、 容積も大きい発泡ポリ ウレタンは、 今後最も厄介な廃棄物処 理の課題といえる。  Since foamed polyurethane is a thermosetting resin, it does not soften or shrink with a heated liquid. So far, no solution capable of reducing the volume and softening has been found. In addition, resilient, large-volume polyurethane foam is one of the most troublesome waste disposal challenges in the future.

発明者は、 本発明のジオール、 ポリオールを適切な温度に加温すれば、 発泡ポ リ ウレタンを減容させ得ることを見出した。 液の温度は 1 5 0 °C以上であること が必要で、 それ以下では減容がおきないか、 又は長時間を要することになる。 一方、 溶液とウレタンの種類にもよるが、 多くの液では、 2 0 0 °C以上の高温 にすると発泡ポリ ウレタンの分解が進行する。 2 0 0 °C以上でも短時間であれば 分解はわずかにと どまるが、 時間の制約のある作業が難しい場合は、 1 5 0〜 2 0 0 °C (グリセロールや、 ポリアルキレングリ コールは 2 3 0 °Cまで可能) まで の間の温度を選択する。 短時間作業が可能な場合でも 2 3 0 °Cが上限といえる。 ただし、 沸点まで加温して蒸気を得、 それを短時間接触させて縮小することも できる。 蒸気にするメ リ ッ トは、 液体が少量ですみ、 かつ減容力が強いわりには 分解はおきにくいためである。 The inventor has found that foaming polyurethane can be reduced in volume by heating the diol or polyol of the present invention to an appropriate temperature. The temperature of the solution must be 150 ° C or higher, below which the volume will not decrease or it will take a long time. On the other hand, depending on the type of solution and urethane, the decomposition of foamed polyurethane proceeds at a high temperature of 200 ° C or more in many solutions. Decomposition is slight in short time even at 200 ° C or higher, but when time-sensitive work is difficult, 150 ° C to 200 ° C (glycerol and polyalkylene glycol are Up to 230 ° C). Even if short-time work is possible, the upper limit is 230 ° C. However, it is also possible to obtain steam by heating it to the boiling point and then contact it for a short time to reduce it. it can. The advantage of using steam is that it requires only a small amount of liquid and does not easily decompose despite its strong capacity for volume reduction.

実験によると、 柔らかい発泡ウレタンは、 ジエチレングリ コールを 1 6 0 °C前 後に加温して、 それに浸し圧縮力を加えると、 分解せずに縮小し、 元に復元しな かった (以下、 この現象を圧縮とよぶ) 。 1 8 0 °Cに熱したジエチレングリ コー ルは、 やや硬めの、 弾力の強い発泡ウレタンであっても、 圧力と併用すれば、 数 分の一に減容した (4 c m厚のものが 5 m mとなった) 。 なお柔らかい発泡ウレ タンについていえば、 プロ ピレングリ コールでは、 1 8 0 °C位において圧縮がで きたが、 同時に分解もかなり短時間でおきた。 ト リエチレングリ コールでは 1 8 0 °C位まで加温すると圧縮が容易であつたが、 分解もわずかに進んだ。 ただし、 完全分解するには、 長時間を要し、 温度もより高温が必要であった。  According to experiments, soft urethane foam shrinks without decomposing when diethylene glycol is heated around 160 ° C and then immersed in it and applies compressive force. This phenomenon is called compression.) Diethylene glycol heated to 180 ° C reduced the volume to a fraction of that of a slightly harder, more resilient urethane foam when used together with pressure. mm). In the case of soft urethane foam, compression of propylene glycol occurred at about 180 ° C, but at the same time, decomposition took place in a very short time. Triethylene glycol was easily compressed when heated to around 180 ° C, but decomposed slightly. However, complete decomposition required a long time and a higher temperature.

圧力は、 溶液と接触している状態でかけるのが好ましいが、 接触後であっても 短時間しか経過していなければ圧縮は可能である。 但し、 加温液と接触させて軟 化した発泡ゥレタンは弾力を失い復元力がなくなるので、 接触後時間が経過して も圧縮することが可能である。  The pressure is preferably applied while in contact with the solution, but compression is possible even after contact if only a short time has elapsed. However, foamed polyurethane softened by contact with the heating liquid loses its elasticity and loses its restoring force, so that it can be compressed even after the elapse of time after contact.

そこで、 柔らかい発泡ウレタンの場合圧縮を容易にし、 分解を最小とするには 、 ジオールと分子量 2 0 0以上の高分子のポリエチレングリ コール、 ポリプロピ レングリ コールなどのポリアルキレンダリ コールとの混液を用い温度を 1 8 0 °C 〜 2 0 0 °Cと高めにするのが好ましい。 ジエチレングリ コールにポリエチレング リ コール (分子量 2 0 0 ) を半分量混合した溶液は 1 8 0 °Cに熱した場合、 分解 はわずかであった。 又、 トリオールであるグリセロールも縮小力が弱いので、 ジ オールとの混液と して分解力を弱める目的で用いるのが望ましい。  Therefore, in the case of soft urethane foam, compression is facilitated and decomposition is minimized by using a mixed solution of diol and polyalkylene glycol such as polyethylene glycol or polypropylene glycol having a molecular weight of 200 or more. Is preferably as high as 180 ° C. to 200 ° C. A solution of a mixture of diethylene glycol and a half amount of polyethylene glycol (molecular weight: 200) showed little decomposition when heated to 180 ° C. In addition, glycerol, which is a triol, also has a weak contracting power, so it is desirable to use it as a liquid mixture with diol for the purpose of weakening the decomposition power.

弾力の強い発泡ウ レタンではジエチレングリ コール又は ト リエチレンダリ コ ールを用い、 ウレタンの材質に応じて 1 7 0度 C以上 2 0 0度 Cまでの間の最適 温度を選び圧触させることが好ましい。  For highly resilient urethane foam, use diethylene glycol or triethylene daryl to select the optimal temperature between 170 ° C and 200 ° C depending on the urethane material, and press it. preferable.

エチレングリ コール、 プロ ピレングリ コール、 ブタンジオール、 ト リエチレン グリ コール、 テ トラエチレングリ コール、 ト リ メチロールプロパン、 グリセリ ン Ethylene glycol, propylene glycol, butanediol, triethylene glycol, tetraethylene glycol, trimethylolpropane, glycerin

、 へキサンジオールなどのジオールやト リオールを減容に用いる場合、 ポリ ウレ タンを高温の溶液に接触させて多少分解が進んだと しても問題はない。 分解物は 原料のダリ コールであるため、 分解物の混入した減容液をポリ ゥ レタ ン再生に利 用できるためである。 従って、 これらのジオール、 ト リ オールを用いる場合、 本 発明は画期的減容法といえる。 When diols such as hexanediol and triol are used for volume reduction, polyurethane There is no problem even if the decomposition of the tin proceeds slightly when the tin is brought into contact with the hot solution. This is because the decomposed product is daricol as a raw material, and the volume-reduced solution containing the decomposed product can be used for regeneration of polyethylene. Therefore, when these diols and triols are used, the present invention can be said to be an epoch-making volume reduction method.

本発明で用いるジオールとは、 アルコール性 O H基を 2個有する化合物、 ポリ オールは O H基を 3個以上有する化合物と定義する。 ジオールには、 グリ コール 類と、 モノアシルグリセロールがある。 グリ コール類は、 メチレン基、 エチレン 基、 プロ ピレン基、 ブチレン基等のアルキレン基に 2つの O H基がついたもので あり 、 具体的には、 エチ レンダリ コールと、 その 2、 3、 4量体のジエチレング リ コール、 ト リエチレングリ コール、 テ トラエチレンダリ コール等が、 又、 プロ ピレングリ コールとその 2量体、 3量体のジプロ ピレングリ コール、 ト リ プロ ピ レンダリ コール等が、 その他ブチル基のブチレンダリ コール、 メチル基の ト リ メ チレングリ コール等がある。 なお、 エチレングリ コールは毒性が強く不適であ り 、 用いる場合は、 閉鎖システムとする必要がある。  The diol used in the present invention is defined as a compound having two alcoholic O H groups, and the polyol is defined as a compound having three or more O H groups. Diols include glycols and monoacylglycerols. Glycols are alkylene groups such as a methylene group, an ethylene group, a propylene group, and a butylene group with two OH groups.Specifically, ethylene glycol and its 2, 3, and 4 Diethylene glycol, triethylene glycol, tetraethylene glycol, and the like, propylene glycol and its dimer and trimer dipropylene glycol, tripropylene glycol, etc., and other butyl groups Butylene glycol, and methylene glycol trimethylene glycol. Ethylene glycol is highly toxic and unsuitable, so if it is used, it must be a closed system.

これらの中で、 ジエチレングリ コール (沸点 2 4 4 °C ) 、 ト リ メチレングリ コ ール ( 2 1 4 °C ) 、 ト リ エチレングリ コール ( 2 8 7 °C ) 、 テ ト ラエチレンダリ コール ( 3 2 7 °C ) 、 ブチレングリ コール ( 2 3 5 °C ) 、 ジプロ ピレングリ コー ル ( 2 3 2 °C ) 、 ト リ プロ ピレングリ コール ( 2 6 8 °C ) が人体への安全性が高 く 、 引火点も高く 、 しかも難燃焼性であるこ とから、 本発明の溶液と して適して いる。 又、 これらの溶液の沸点は高く 、 ほとんどのプラスチック材を軟化するこ とが可能である。  Among them, diethylene glycol (boiling point: 244 ° C), trimethylene glycol (2144 ° C), triethylene glycol (287 ° C), tetraethylene glycol (3 (27 ° C), butylene glycol (235 ° C), dipropylene glycol (232 ° C), and tripropylene glycol (268 ° C) are highly safe for humans. Since it has a high flash point and is difficult to burn, it is suitable as the solution of the present invention. In addition, the boiling points of these solutions are high, and most plastic materials can be softened.

その他、 本発明ではジオールに含めたダリ コール類の重合体である高分子のァ ルキレングリ コール類も加温時に減容カを有する。 例えば、 ポリエチレングリ コ ール、 ポリ プロ ピレングリ コールなども発泡材ゃプラスチック容器を縮小し、 プ ラスチック材を軟化させる。 これらは高温でも揮発しにく いという点において他 のジォ一ル、 ト リ オールよ り も優れている。 ただし、 粘性があり 、 付着液を除去 しにくいとレ、う欠点がある。 ポリ プロ ピレングリ コールは液体であるが、 ポリエ チレングリ コールでは分子量 1 0 0 0以上のものは室温で固体であるので、 それ 以下のものが取り扱いの点から好ましい。 In addition, in the present invention, high molecular weight alkylene glycols, which are polymers of dalicols included in the diol, also have a reduced volume when heated. For example, polyethylene glycol, polypropylene glycol, etc. also reduce the size of the foam / plastic container and soften the plastic material. They are superior to other giols and triols in that they are less volatile at high temperatures. However, there is a drawback that it is too viscous to remove the adhering liquid. Polypropylene glycol is a liquid, but polyethylene glycol with a molecular weight of 1000 or more is a solid at room temperature. The following are preferred in terms of handling.

ポリオールのうち、 ト リオールも減容に有用である。 ト リオールには、 グリセ リ ン、 ト リ メ チロー レエタン、 ト リ メ チローノレプロパン、 ソノレビ トーノレ、 マンニ トールなどの ト リオールがある。 これらは、 固体であるが本発明の他の液体を混 ぜて加温すれば液体となる。 トリ メチロールプロパンについては、 融点が 5 9 °C であるので、 加熱により容易に液体となり、 沸点は 2 9 2 °Cであるので揮発しに く く、 さ らに人体安全性、 環境安全性が高い等の長所がある。 また、 グリセリ ン は、 人体安全性は高く、 引火点も極めて高く、 燃焼性が弱い。 Among polyols, triol is also useful for volume reduction. Triols include glycerin, trimethylol ethane, trimethylolone propane, sonolevi tonole, mannitol, and other triols. These are solids, but become liquids when mixed with the other liquids of the present invention and heated. Trimethylolpropane has a melting point of 59 ° C, easily turns into a liquid by heating, and has a boiling point of 292 ° C, which makes it difficult to volatilize, further reducing human and environmental safety. There are advantages such as high. Glycerin is also highly safe for humans, has an extremely high flash point, and has low flammability.

ぺッ トボトル及ぴ、 そのチップを減容する液にエチレンダリ コールを用いた場 合、 洗浄を不要とすることも可能である。 エチレング.リ コールはペッ トボトルの 原料であるため、 使用後の減容液はぺッ トボトルを分解するリサイクルエ程に組 み入れることができる。  If ethylene dalicol is used for the bottle and the liquid for reducing the volume of the chip, washing can be eliminated. Since ethylene glycol is a raw material for pet bottles, the volume-reduced liquid after use can be incorporated into the recycling process for disassembling pet bottles.

本発明の廃材の処理装置は、 まず減容液を所定の温度に加熱する装置が必要で ある。 加熱する装置は、 液をかける方式、 すなわち、 ふりかけたり、 シャ ワー状 に流したり、 また自然落下させる方式の場合は、 液の流出口の直前に設置しても 良い。 又、 吹きかける方式、 すなわち、 高圧空気とともに液を噴射したり、 スプ レーしたりする方式も液の流出口の直前であって良い。 もし直前でない場合は、 加熱部と流出口までの管は、 熱が逃げないよ うに、 断熱とするのが好ましい。 大きなタンクの中に溶液を満たし、 その中に廃材を入れタンクの中の液を加熱 する方式の場合は、 タンクを直接加熱するか、 タンク と加熱部を別にして循環さ せる方法がある。 タンク式では、 廃材を加温した液に浸すか、 浸した後溶液を加 温するかいずれかになる。 該回収装置は、 種々の廃材に適用できることが好まし く、 従ってさ らに圧力を加えることができる装置が必要である。  The apparatus for treating waste material of the present invention first requires an apparatus for heating the volume reducing solution to a predetermined temperature. In the case of a system for applying a liquid, that is, a method of applying a liquid, that is, a method of sprinkling, flowing in a shower shape, or a method of allowing the liquid to fall naturally, the heating device may be installed immediately before the liquid outlet. Further, the spraying method, that is, the method of spraying or spraying the liquid together with the high-pressure air may be provided immediately before the liquid outlet. If not immediately before, the pipe to the heating section and the outlet is preferably insulated so that heat does not escape. When a large tank is filled with a solution and waste material is put into the tank to heat the liquid in the tank, the tank can be heated directly or the tank and heating section can be circulated separately. In the tank type, either the waste material is immersed in a heated solution or the solution is heated after immersion. Preferably, the recovery device can be applied to various kinds of waste materials, and therefore, a device capable of further applying pressure is required.

圧力は一般には、 圧縮力であり、 ピス ト ン方式、 プレス方式などがある。 圧縮 力は、 減容物を加温液に浸しながら、 又は加温液をかけながら加えるのが効率が よい。 ただし、 圧力は、 浸した液から取り出した直後、 加温液をかけた直後、 も しく は溶液を止めた直後であってもよい。  The pressure is generally a compressive force, and includes a piston method, a press method, and the like. It is efficient to apply the compressive force while immersing the volume-reduced material in the heating liquid or applying the heating liquid. However, the pressure may be immediately after removal from the soaked solution, immediately after applying the heating solution, or immediately after stopping the solution.

前述の高圧スプレー、 高圧噴射方式では同時に圧力をかけるので、 発泡スチロ 1 ール、 ペッ トボ トルの本体部分のように、 減容に弱い圧力で足り る場合には、 特 別な加圧装置は不要である。 In the high-pressure spray and high-pressure injection methods described above, pressure is applied at the same time. No special pressurizing device is needed when pressure is weak enough to reduce the volume, as in the case of a 1-bar or pet bottle body.

最後には、 減容した廃材は、 集められる。 上から液をふりかけて減溶する方式 では、 ベルトコンベアに載って移動せられ、 収集用の箱の中に入れる。 タンク式 では、 網かごがタンクの中に浸かっていて、 それが引き上げられ、 かごに集めら れる。  Finally, the reduced volume waste is collected. In the method in which the solution is sprinkled from above to reduce the dissolution, it is moved on a belt conveyor and placed in a collection box. In the tank type, a net basket is submerged in the tank, which is raised and collected in a basket.

加温には、 灯油、 プロパンガス、 都市ガスにより、 液を加温する方式と、 電熱 加熱方式が一般的に使用されるが、 本発明の溶液はすべて高周波誘導加熱、 マイ ク ロ波加熱、 超音波加熱、 高周波振動加熱、 超音波振動加熱等により、 急速に加 熱が可能である。 又、 赤外線加熱、 遠赤外線加熱も可能である。 特に高周波振動 加熱、 超音波振動加熱は、 装置がコンパク トになり、 かつ、 火災の危険がないこ とから好ましい。 ここで超音波加熱とは、 1 . 6万 Hz以上の超音波を照射するこ とをいうが、 照射時間と強度により数千 Hzの高周波振動でも加熱が可能である。 マイクロ波加熱、 超音波加熱、 超音波振動加熱は、 熱源を使用しないため装置 がコンパク トとなり、 火災の危険がないという優れた特徴を有する。 超音波を用 いる装置のコンパク ト化は、 液をふりかけたり、 吹きかけたり、 スプレーしたり する方式で特に顕著となる。 なぜなら、 超音波は局部的に照射すれば液温は瞬時 に上昇するので、 これらの方式において、 ノズル手前で照射すればよいので、 加 熱部がコンパク トとなる。  For heating, a method of heating the liquid with kerosene, propane gas, or city gas and an electric heating method are generally used, but the solutions of the present invention are all high-frequency induction heating, micro wave heating, Rapid heating is possible by ultrasonic heating, high frequency vibration heating, ultrasonic vibration heating, etc. Infrared heating and far infrared heating are also possible. In particular, high-frequency vibration heating and ultrasonic vibration heating are preferable because the equipment becomes compact and there is no danger of fire. Here, the ultrasonic heating means irradiating an ultrasonic wave of 16,000 Hz or more, but heating can be performed by high frequency vibration of several thousand Hz depending on irradiation time and intensity. Microwave heating, ultrasonic heating, and ultrasonic vibration heating have the advantage that the equipment is compact because there is no heat source and there is no danger of fire. The compaction of equipment using ultrasonic waves is particularly remarkable in systems in which liquid is sprinkled, sprayed, or sprayed. The reason is that the liquid temperature rises instantly if the ultrasonic wave is applied locally, so in these methods, it is sufficient to irradiate just before the nozzle, and the heating unit becomes compact.

以下、 本発明に係る減容 · 軟化装置を添付図面を参照して詳述する。  Hereinafter, a volume reducing / softening device according to the present invention will be described in detail with reference to the accompanying drawings.

第 1図に示すように、 減容タンク 4は上下に分かれており、 上部に加熱器 8を 通して加温された減容液 1を入れたタンクがあり、 そこへ発泡材ゃぺッ トボトル 9を入れ、 上方から加圧機 1 0で、 廃材を液中に沈めながら平らな網部 2 とはさ むよ うに加圧減容する。 減容後は、 バルブ 5を開き、 液をタンク下部の廃溶液だ め 3に落とす。再び加圧機が降りて溶液を絞り出す。加圧機が上に引き上げられ、 次に網部も上に引き上げられ廃材が収集される。 ポンプ 6を作動させ、 加熱器 8 へタンク下部の溶液を送り加温する。 加熱された液は噴射口 7より上方からタン クに注がれ、 タンクに先に新しい廃材が入れられる。 先に、 タンクに廃材が入れられ、 次に、 上方から加熱された液が噴射口よりス プレーされる方式でも良い。 As shown in Fig. 1, the volume reduction tank 4 is divided into upper and lower parts, and there is a tank containing the volume reduction liquid 1 heated through a heater 8 at the upper part. 9 and pressurize it with a press 10 from above to reduce the volume while submerging the waste material in the liquid and sandwiching it between the flat nets 2. After reducing the volume, open valve 5 and drop the liquid into waste tank 3 at the bottom of the tank. The press again descends and squeezes the solution. The press is lifted up, then the net is also lifted up and the waste is collected. Activate the pump 6 and send the solution under the tank to the heater 8 to heat it. The heated liquid is poured into the tank from above the injection port 7, and new waste is put into the tank first. First, waste material is put into the tank, and then the liquid heated from above is sprayed from the injection port.

溶液がボトルの中に入ると、 減容後、 ボトルの中に入った溶液を廃出するのが 困難となる。 その場合減容したボトルに穴をあけるか、 数ケ所切断して液を出す ことができる。  Once the solution is in the bottle, it is difficult to drain the solution in the bottle after reducing the volume. In that case, you can make holes in the reduced volume bottle or cut several places to discharge the liquid.

第 2図のよ うにポトル 1 6を横に整列させて置き、 細孔 1 4から加温液を加え ながら上から加圧して庄縮する。 このボトルを横に寝かせ、 全体を圧縮する方式 は、 溶液がボトル内に入りにく く、 ボトルの方向をそろえる必要はない。 この図 を詳しく説明すると、 空気圧縮機 1 9により溶液タンク 1 8内の減容液を上方に 送り、 超音波加熱器 1 1で加温し、 圧縮機内の空間に注入する。 溶液は圧縮面 1 3の下部の細孔 1 4より出て、 下方に落ち、 ぺッ トボトル 1 6にかかり、 下方の 底板 1 7へ落下する。 同時に、 圧縮面 1 3を下げ、 軟化したぺッ トボトルを下方 へ圧縮する。 次に、 縮小したペッ トボトルを上方から取り出す。 なお、 ドレイ ン 1 5からの廃液は、タンク 1 8に戻してよい。  As shown in Fig. 2, the potters 16 are placed side by side, and pressurized from above while adding a heating liquid from the pores 14 to constrict. This method of laying the bottle on its side and compressing the entire body makes it difficult for the solution to enter the bottle and there is no need to align the bottle. More specifically, the volume reducing solution in the solution tank 18 is sent upward by the air compressor 19, heated by the ultrasonic heater 11, and injected into the space in the compressor. The solution emerges from the pores 14 below the compression surface 13, falls down, falls on the bottle 16, and falls down to the bottom plate 17. At the same time, the compression surface 13 is lowered, and the softened bottle is compressed downward. Next, remove the reduced pet bottle from above. The waste liquid from the drain 15 may be returned to the tank 18.

第 3 ( a ) 図のように、 ベルトコンベアにより、 ペッ トボトルが送られてきて 、 ぺッ トボ トルの口部分と底部分のみを同時に押しつぶされるよ うに圧縮機が下 におり る。 この時、 圧縮機底面の孔から加熱した溶液 2 1がふりかけられる。 加 熱には、 圧縮板 1 0内への液の注入部直前に超音波加熱器 1 1がつけられている 。 ペッ トボ トルの場合、 ボ トルの中間部は、 圧力がかからなく とも、 溶液がかか るだけで収縮し、 加温した溶液に接触させ、 圧力をかければ、 口部と底部をも押 しつぶし平らにすることができる。 この時、 中間部は収縮が起きるので、 圧力の みよ り も大きな減容率を得ることができる。 第 3 ( b ) 図のように、 底面は平ら でも良い。 これは発泡スチロールにも適用できる。  As shown in Fig. 3 (a), the compressor is lowered so that the pet bottle is sent by the belt conveyor and only the mouth and bottom of the pet bottle are crushed at the same time. At this time, the heated solution 21 is sprinkled from the hole on the bottom of the compressor. For heating, an ultrasonic heater 11 is provided immediately before the liquid is injected into the compression plate 10. In the case of a pet bottle, the middle part of the bottle shrinks only by the application of the solution, even if no pressure is applied, so that it comes into contact with the heated solution, and if pressure is applied, the mouth and bottom are also pressed. Can be flattened. At this time, since the middle part shrinks, a greater volume reduction rate can be obtained than with pressure alone. The bottom surface may be flat as shown in Fig. 3 (b). This can be applied to styrofoam.

なお、 ボトルの集合から 1つを選別するにはいろいろな方法があるが、 工場で よく使われるベル トコンベア方式が最も単純である。  There are various methods to select one from a set of bottles, but the belt conveyor method often used in factories is the simplest.

分別が行えるよ う設計した回収装置では、 発泡材及びプラスチック材を区別す ることなく上記溶液の入った容器に入れ、 上記加熱溶液をこれらに吹き付け、 比 重や流動性、 大きさをもとに分別し、 分別収集を自然に行う ことが可能である。 タンク式では、 第 4図のように、 塩化ビュルとポリエステルを除く、 ほとんどの プラスチック 9 (ペッ トボトルは、 中に必ず空気が残っているので浮くが、 溶液 で完全に満たせば沈む) は、 ジオールの表面に浮力により淳いているので、 コン ベア 2 5で斜め上方へ一つ一つ引き上げて収集することもできる。 In a recovery device designed to perform separation, the foamed material and the plastic material are placed in the container containing the solution without distinction, and the heated solution is sprayed on them, Sorting based on weight, fluidity, and size allows for separate collection naturally. In the tank type, as shown in Fig. 4, most of the plastics 9 except petroleum chloride and polyester (Pet bottles float because there is always air inside, but sink when filled completely with solution) are diols It can be collected by pulling it up diagonally upward on conveyor 25 as it is in contact with the surface of the building by buoyancy.

回収装置は、 スーパーマーケッ ト、 コ ンビニエンスス トア、 あるいは市町村の 収集場所に設置される。 これら収集場所から集められた廃プラスチック材は、 巿 町村や廃棄物処理業者等に引き取られる。 この際、 その重量に応じて引き取り価 格が定められている。 従って、 本発明によれば、 廃プラスチック材の縮小度合い が大きいために、 一度に多量の廃プラスチックを運搬でき、 よって運搬業者にと つて一度の回収でより多くの収益を得ることができる。  Collection equipment will be installed at supermarkets, convenience stores, or municipal collection points. Waste plastic materials collected from these collection sites are collected by municipalities and waste disposal companies. At this time, the pickup price is determined according to the weight. Therefore, according to the present invention, a large amount of waste plastic can be transported at one time because the degree of reduction of the waste plastic material is large, and therefore, more profits can be obtained for the carrier in one recovery.

本発明の方法によって得られた発泡スチロールの減容物は、 水洗によって、 付 着した液を除去した後、 乾燥させ、 それを適当な大きさのペレッ トと し (発泡ス チロールの段階で、 あらかじめ適当な大きさに細分しておけば、 減容した時点で は、 1つ 1つが適当なペレッ トとなっていることも可能) 、 減圧状態で押出し成 形機にかけて再びポリ スチレンを得ることができる。 もし、 .減容液の温度を 2 0 0 °Cを超えないようにすれば、 熱変性も生じにく く、 良好な物性のポ リ スチレン が再生される。  The reduced volume of styrofoam obtained by the method of the present invention is obtained by removing the attached liquid by washing with water, and then drying it to obtain a pellet of an appropriate size (at the stage of styrofoam, If the volume is reduced to an appropriate size, it is possible that each pellet will have an appropriate pellet at the time of volume reduction), and it will be possible to obtain polystyrene again by using an extrusion molding machine under reduced pressure. it can. If the temperature of the volume-reducing liquid does not exceed 200 ° C, thermal denaturation is unlikely to occur, and polystyrene with good physical properties is regenerated.

ジオール又はポリオール中に本発明によって減容したプラスチック又は減容 前のプラスチックを混合した時、 発泡スチロール及びポリエチレン、 ポリプロピ レン等の容器、 板、 シート、 不織布等は液面に浮かぶ。 滅容して内部が溶液で満 ちたペッ トボトル、 ポリエステル又は塩ビ製の板、 シート等は底に沈む。 そこで 、 まず発泡スチロール、 ポリエチレン、 ポリプロピレン等をすくい取る力 液上 層を流し出して取り出し、 次にポリエステルと塩化ビエルを取り出し、 これらを 分別することができる。  When a plastic reduced in volume according to the present invention or a plastic before volume reduction is mixed in a diol or a polyol, a container, a plate, a sheet, a nonwoven fabric, or the like such as styrene foam and polyethylene or polypropylene floats on the liquid surface. Pet bottles, polyester or PVC plates, sheets, etc., which are destroyed and filled with solution, sink to the bottom. Therefore, first, a force for scooping styrofoam, polyethylene, polypropylene and the like is poured out and taken out, and then polyester and bichloride are taken out, and these can be separated.

次に、 本発明の別の実施態様を示すと、 前記軟化減容液 (各々縮小液を混合し て、 特性をもたせてもよい) の温度を 1 3 0〜 2 0 0 °C程度にするのが良い。 こ の温度にするのは、 処理ス ピー ドを上げるのと、 プラスチックの対象を多くする 4 ためである。 次に、 そこに発泡材の断片又はプラスチック材、 あるいはボトルな どの容器を同じ収容容器に入れ又は別々の収容容器に入れ、 かき混ぜるか、 断片 を溶液中に押し込むなどして液と十分に接触させる。 この時、 圧力を加えると減 容を早めることができる。 強い圧力を加えれば、 減容率を大きく しかつさらなる 処理スピー ドのアップが可能となる。 Next, according to another embodiment of the present invention, the temperature of the softening and volume reducing solution (each of which may be mixed with a reducing solution to give characteristics) is set to about 130 to 200 ° C. Is good. This temperature increases the processing speed and increases the amount of plastics 4 That's why. Next, put a container such as a piece of foam material or plastic material, or a bottle in the same container or in a separate container, and stir or push the fragment into the solution to make sufficient contact with the liquid. . At this time, applying pressure can speed up the volume reduction. Applying strong pressure can increase the volume reduction rate and further increase the processing speed.

減容したら、 それを網ですくいとるカ 液を別のタンクに移動させ、 底部の網 上に残った減容 *発泡材ゃプラスチック材を水洗するか、 圧縮機に移しさらに強 力な圧力を加えて液をしぼり出す。 最後に洗浄する必要がある場合は、 水洗によ り溶液を洗い流す。 単なる洗い流しの他に、 ジェッ ト洗浄や、 超音波洗浄を行つ てもよい。 次に、 取り出した発泡材、 プラスチック材を乾燥する。 この後、 減容 されたプラスチック材は、 切断機で細かく切断される。  When the volume is reduced, remove it with a net and transfer the liquid to another tank.Reduce the volume remaining on the bottom net. * Wash the foam material ゃ plastic material with water or transfer it to a compressor to apply even stronger pressure. In addition, squeeze out the liquid. If final cleaning is required, flush the solution with water. In addition to mere washing, jet cleaning and ultrasonic cleaning may be performed. Next, the removed foam and plastic materials are dried. After this, the reduced plastic material is finely cut by a cutting machine.

前述のように、 発泡材、 ボトル、 容器、 かさ高のシートや、 不織布を最大限に 減容させるためには、 圧縮機による圧縮を併用する。 圧力を大きくすれば、 内部 の液をしぼり出すことができる。  As mentioned earlier, in order to reduce the volume of foams, bottles, containers, bulky sheets and non-woven fabrics as much as possible, compression by a compressor is also used. If the pressure is increased, the liquid inside can be squeezed out.

減容 '軟化液は、 単独である必要はなく、 燃焼性、 流動性、 沸点、 加熱の難易 、 対象プラスチックなどを考慮して混合して用いてもよい。  The volume-reducing softening liquid does not need to be used alone, and may be used as a mixture in consideration of flammability, fluidity, boiling point, difficulty of heating, target plastic, and the like.

本発明によれば、 温度を高く し、 圧縮力を組み合わせることにより、 熱硬化性 樹脂以外のほとんどのプラスチックを減容又は軟化できる。 発泡スチロール、 ぺ ッ トボ トル、 ポリエチレン容器等に限定すれば、 比較的低温でも減容又は軟化が 可能である。 また、 ペッ トボ トルの減容液はポリエステルの原料にでき、 発泡ポ リ ウレタンを減容し、 その時の減容液をポリ ウレタンの原料にできるなど、 リサ ィクルに可能である。  According to the present invention, most plastics other than the thermosetting resin can be reduced in volume or softened by increasing the temperature and combining the compressive force. If limited to polystyrene foam, water bottles, polyethylene containers, etc., the volume can be reduced or softened even at a relatively low temperature. In addition, PET bottles can be used as a raw material for polyester to reduce the volume of foamed polyurethane, and the reduced volume at that time can be used as a raw material for polyurethane.

リサイクルシステムによれば、 上述した回収装置により回収した廃プラスチッ ク材の重量に応じて引き取り価格が決められる。  According to the recycling system, the collection price is determined according to the weight of the waste plastic material collected by the above-mentioned collection device.

また、 リサイクルシステムによれば、 発泡材、 プラスチック容器、 ペッ トボト ル又はプラスチック材等の廃プラスチック部材を収集して上述した減容又は軟化 方法、 上述した回収装置により廃プラスチック部材を処理して作られた再生ブラ スチッタ材を原料と して再製品が作られる。 5 上述した減容又は軟化方法、 及び上述した回収装置により処理した発泡材、 プ ラスチック容器、 ペッ トボトル又はプラスチック材等の廃プラスチック部材を原 料と してシリ ンダー内減圧装置を備えた押出成形機又は射出成形機により成形す る。 In addition, according to the recycling system, waste plastic members such as foam materials, plastic containers, pet bottles, or plastic materials are collected, and the volume is reduced or softened as described above. Remanufactured products are made from the recycled blasting materials. (5) Extrusion molding using a waste plastic member such as a foam material, plastic container, plastic bottle, or plastic material treated by the above-mentioned volume reduction or softening method and the above-mentioned recovery device and equipped with a decompression device in a cylinder It is molded by a press or an injection molding machine.

ジオール又はポリオールとプラスチック廃材とを混合し、 液面にあるもの と、 液中又は底に沈むものに分けた後、 それぞれを回収する。  Mix the diol or polyol with plastic waste and separate them into those at the liquid surface and those that sink into the liquid or at the bottom, and then collect each.

実施例 1  Example 1

プロピレング ール 1 0 0 m 1 を、 電子レンジ ( 5 0 0 W) で 2分マイク口 波加熱した。 その時液温は 1 2 0でであった。 そこに、 発泡スチロール断片を入 れ、 棒で溶液中に押し込み圧力を加えると、 気泡が出て減容した。  Propylene grease 100 m1 was heated by microwave in a microwave oven (500 W) for 2 minutes. At that time, the liquid temperature was 120. The styrofoam fragments were put into it, and they were pushed into the solution with a stick and pressure was applied.

実施例 2  Example 2

グリセローノレ 1 0 0 m 1 を用いて電子レンジ加温し、 液温 1 2 5〜 1 5 0でと し、 実施例 1 と同核にして減容した。  The mixture was heated in a microwave oven using 100 ml of Glyceronore, and cooled to a liquid temperature of 125 to 150. The volume was reduced to the same nucleus as in Example 1.

実施例 3  Example 3

ジプロピレングリ コール 1 0 O m l にっき、 電子レンジで 1分加温して 1 3 0 Dipropylene glycol 10 O ml, heated in a microwave for 1 minute, 130

°Cと し、 そこに 、 発泡スチ口ール小断片を入れ減容した。 ° C, and put a small piece of styrofoam there to reduce the volume.

実施例 4  Example 4

ポリプロピレングリ コール (分子量 3 0 0 ) 1 0 0 m l を電子レンジで加温し て 1 3 0 °Cと し 、 そこに発泡スチロール小断片を入れ減容した。  100 ml of polypropylene glycol (molecular weight: 300) was heated to 130 ° C. in a microwave oven, and a small piece of styrofoam was put therein to reduce the volume.

実施例 5  Example 5

ポリエチレング y コール (分子量 4 0 0 ) 1 0 0 m 1 を電子レンジで加温して Polyethylene glycol (molecular weight: 400) 100 m1 is heated in a microwave oven

、 1 7 0 °Cと し 、 そこに発泡スチロール小断片を入れ、 瞬時に減容した。 The temperature was set to 170 ° C, and a small piece of styrofoam was put therein, and the volume was reduced instantaneously.

実施例 6  Example 6

ポリプロピレングリ コール (分子量 4 0 0 0 ) 1 0 0 m l を電子レンジで 2分 加温して 1 8 5 と し、 そこに発泡スチロール小断片を入れ、 瞬時に減容した。 また、 ポリェチレン製プロック 1 0 gを軟化させた。  100 ml of polypropylene glycol (molecular weight: 400,000) was heated in a microwave oven for 2 minutes to a temperature of 185, and a small piece of styrofoam was added thereto, and the volume was reduced instantaneously. In addition, 10 g of polyethylene block was softened.

実施例 7  Example 7

軟質発泡ポリゥレタンを、 電熱加熱したジエチレングリ コール ( 1 7 0 °C) 中 6 につけ、 5分放置して軟化させた。 次に、 液を別の容器に移し、 上から押しつけ て軟性発泡ウレタンを減容させた。 又、 ポリ プロ ピレン 1 0 gを軟化させた。 Soft foamed polyurethane in diethylene glycol (170 ° C) heated electrically 6 and left for 5 minutes to soften. Next, the liquid was transferred to another container and pressed from above to reduce the volume of the flexible urethane foam. Also, 10 g of polypropylene was softened.

実施例 8  Example 8

ト リメチロールエタン粉末 2 2 5 gに トリエチレンダリ コール 3 0 gを加え、 ホッ トプレー トで加熱して液体と し 1 3 0 °Cと した。 この溶液に発泡スチロール の断片を入れ減容した。  To 25 g of trimethylolethane powder, 30 g of triethylene dalicol was added, and the mixture was heated to 130 ° C by heating with a hot plate. Styrofoam fragments were put into this solution to reduce the volume.

実施例 9  Example 9

ジエチレングリ コール 1 O m l と ト リエチレングリ コール 1 O m l の混合液を 電子レンジで 1 8 まで加熱し、 ここへ発泡ポリ ウレタンを約 1分つけて軟化 させ、 取り出して吸水液を押さえて除いた。 このものは再ぴふく らむことはなく 、 減容したままであった。  A mixture of 1 O ml of diethylene glycol and 1 O ml of triethylene glycol was heated to 18 in a microwave oven, and the foamed polyurethane was softened by pouring it for about 1 minute, then removed, and the absorbent was pressed down and removed. . This one did not reappear, and the volume was reduced.

実施例 1 0  Example 10

プロピレングリ コール、 ジプロピレングリ コール各々約 5 0 m 1 をジーエルサ ィエンス製超音波洗浄器 U S 1 0 0 ( 4 5 k H z ) に入れ、 超音波照射し照射部 液温を 1 1 0 °Cと し、 発泡スチロール断片を、 照射部中央におき減容した。  Approximately 50 m1 of propylene glycol and dipropylene glycol are each placed in a US 100 (45 kHz) ultrasonic cleaner manufactured by GL Sciences, and irradiated with ultrasonic waves to adjust the temperature of the irradiated part to 110 ° C. However, a piece of styrofoam was placed in the center of the irradiated area to reduce the volume.

実施例 1 1  Example 11

ト リエチレンダリ コールを 1 4 0。Cと し、 発泡スチロール小片を 1 0秒で 1 / 3 0に減容した。  140 for triethylene dali coal. As C, the styrofoam pieces were reduced to 1/30 in 10 seconds.

実施例 1 2  Example 1 2

ポリエチレンダリ コール (分子量 6 0 0 ) を 5 0 O mlビーカーに入れ、 液温を 1 6 0 °Cと し、 そこに炭酸飲料用の硬質ペッ トボトルを立てて入れ、 軽く下に押 しながら減容させた。  Polyethylene dalicol (molecular weight: 600) is placed in a 50 O ml beaker, the liquid temperature is set to 160 ° C, and a hard PET bottle for carbonated drinks is set up in the beaker. Allowed.

実施例 1 3  Example 13

ジエチレングリ コールをビーカーにと り、 電子レンジ ( 5 0 0 W) にて加温し て 1 7 0 °C位と し、 そこに発泡ポリ ウレタンを 1 0 c m 3程度入れた。 しばらく すると膨潤するが数分で軟化したので取り出し、 吸水紙の上に置いて上から押さ えると減容し、 再び膨らむことはなかった。 Diethylene glycol was placed in a beaker, heated in a microwave oven (500 W) to about 170 ° C., and about 10 cm 3 of foamed polyurethane was put therein. After swelling for a while, it softened in a few minutes, so it was taken out, placed on water-absorbent paper and pressed from above to reduce the volume, and did not swell again.

実施例 1 4 7 ジエチレングリ コール 2 0 m l にテ トラエチレングリ コールを 1 0 m l ビー カーに入れてまぜ電子レンジで 1 8 0 °Cに加温した。 そこに、 1 0 c m3程度の 発泡ポリ ウレタンを入れた。 実施例 1 4 と同様に 1 〜 2分で軟化し、 押さえて減 容させた。 Example 14 7. Add 20 ml of tetraethylene glycol to 20 ml of diethylene glycol, mix, and heat to 180 ° C in a microwave oven. There, about 10 cm 3 of foamed polyurethane was put. As in Example 14, softening was performed in 1 to 2 minutes, and the volume was reduced by pressing.

実施例 1 5  Example 15

テ トラエチレンダリ コールを 1 8 0 に加温し、 同様にして、 発泡ポリ ウレタ ンを軟化させ、 圧力を加えて押さえて縮小させた。  Tetraethylene dalicol was heated to 180, and the foamed polyurethane was softened in the same manner and reduced by applying pressure.

実施例 1 6  Example 16

5 X 5 X 5 c mの立方体の鉄を 2個用意し、 それを木に結び付け中央に木の口 ッ ドを取り付けた。 次に 1 8 0 °Cに熱したト リエチレングリ コールを、 横にねか せたぺッ トボトルにかけて真ん中部を縮小させると ともに、 口部と底部は十分に 液をかけ柔らかく なった口部と底部に、 ロッ ドを手に持ってこの圧縮機を押し付 けて圧縮した。  Two 5 x 5 x 5 cm cubes of iron were prepared, tied to a tree, and a wooden mouth was attached in the center. Next, triethylene glycol heated to 180 ° C was placed on a side-walled bottle to reduce the size of the middle part, and the mouth and bottom were sufficiently filled with liquid to soften the mouth. The compressor was pressed against the bottom by pressing the compressor with the rod in hand.

実施例 1 7  Example 17

テ トラエチレングリ コールを 1 7 0 °Cに加温し、 炭酸飲料用ぺッ トポトルを横 にねかせて、 加熱液体を上から注ぎながら、 メラミン製の板で上から圧力をかけ て圧縮した。 ペッ トボトルの口部と底部は極めて硬く、 圧力のみではつぶれない 。 しかし、 1 7 0 °Cの液をかけながらであれば、 人の手で上から押さえつけるだ けでも、 口部と底部を押しつぶすことができた。 直径 7 c m、 長さ 2 1 c m、 口 部直径 3 c mのぺッ トボ トルが、 厚み 1 c m長さ 1 3 c mの平板状に減容された 。 この減容率は他のいかなる減容法にもまさるものである。  Tetraethylene glycol was heated to 170 ° C, and the carbonated beverage pot was laid sideways, and the heated liquid was poured from above and compressed by applying pressure from above on a melamine plate. The mouth and bottom of the PET bottle are extremely hard and cannot be crushed by pressure alone. However, while the liquid at 170 ° C was applied, the mouth and bottom could be crushed simply by pressing with human hands from above. A pet bottle with a diameter of 7 cm, a length of 21 cm, and a mouth diameter of 3 cm was reduced to a flat plate having a thickness of 1 cm and a length of 13 cm. This volume reduction rate is superior to any other volume reduction method.

実施例 1 8  Example 18

テ トラエチレンダリ コールを 1 7 0 °Cに加温し、 それを発泡スチロールにかけ た結果、 圧力をかけなく とも急速に減容した。 一般に、 1 3 0 °C以上に加温した 液体であれば、 発泡スチロールの減容に圧力は不要である。 産業上の利用可能性 8 本発明に最適な対象は、 発泡材では発泡スチロール及び発泡ポリエチレンであ る。 容器では、 ペッ トボ トル、 ポリ エチレン容器、 ポリ プロ ピレン容器、 塩ビ容 器などに適用できる。 さ らに、 プラスチック材であるポリエチレン製、 塩ビ製、 ポリ プロ ピレン製、 ポリエステル製の板、 筒、 シー ト、 不織布、 布、 繊維の束な どを軟化するこ と も容易である。 発泡材、 プラスチック容器、 ペッ トボ トル又は プラスチック材等の廃プラスチック部材を収集して再生プラスチック材を原料と して再製品を作る リ サイ クルシステムに適用できる。 これらは、 現代社会で最も 需要の多いものである。 Heating tetraethylene dalicol to 170 ° C and applying it to styrofoam resulted in a rapid volume reduction without pressure. In general, if the liquid is heated to 130 ° C or higher, no pressure is required to reduce the volume of styrofoam. Industrial applicability 8 The most suitable objects for the present invention are styrofoam and polyethylene foam in the case of foam materials. For containers, it can be applied to pet bottles, polyethylene containers, polypropylene containers, and PVC containers. In addition, it is easy to soften plastics such as polyethylene, PVC, polypropylene, and polyester plates, tubes, sheets, nonwoven fabrics, cloths, and fiber bundles. The system can be applied to a recycling system that collects waste plastic materials such as foam materials, plastic containers, pet bottles, and plastic materials, and uses recycled plastic materials as raw materials to produce products. These are the most in demand in modern society.

Claims

請求の範囲 The scope of the claims 1 . ジオール又はポリオールの溶液もしくはそれらの混合液を所定の温度に加 熱し、 該加熱溶液に発泡材、 プラスチック容器又はプラスチック材を接触させて 減容又は軟化させ、 同時に又は後で該発泡材、 プラスチック容器又はプラスチッ ク材を収集してなる廃材の回収方法。 1. Heat a diol or polyol solution or a mixture thereof to a predetermined temperature, and contact a foaming material, a plastic container or a plastic material with the heated solution to reduce or soften the volume, simultaneously or later, with the foaming material, A method for collecting waste materials collected from plastic containers or plastic materials. 2 . ジオール又はポリオールの溶液もしく はそれらの混合液と発泡材、 プラス チック容器又はプラスチック材を接触させた状態で、 もしく は接触させながら溶 液を加熱して減容又は軟化させ、 同時に又は後で該発泡材、 プラスチック容器又 はプラスチック材を収集してなる廃材の回収方法。  2. While the diol or polyol solution or a mixture thereof is in contact with the foaming material, plastic container or plastic material, or while the solution is heated, the solution is heated to reduce or soften the volume. Or, a method of collecting waste material by collecting the foamed material, plastic container or plastic material later. 3 . 前記接触時に又は接触直後に圧力を加えることを特徴とする請求項 1又は 2記載の廃材の回収方法。  3. The method for collecting waste material according to claim 1, wherein a pressure is applied at the time of or immediately after the contact. 4 . 前記溶液温度を 8 0 °C以上から沸点までの範囲内の温度に加熱することを 特徴とする請求項 1又は 2記載の廃材の回収方法。  3. The method for recovering waste materials according to claim 1, wherein the temperature of the solution is heated to a temperature within a range from 80 ° C. or higher to a boiling point. 5 . 前記発泡材は、 発泡スチロール又は発泡ポリ エチレンであり、 前記プラス チック容器は、 ポリ エチレン製、 ポリ プロ ピレン製、 又はポリ塩化ビュル製の容 器、 もしくはペッ トボトルであり、 前記プラスチック材は、 ポリ塩化ビュル製、 ポリエチレン製、 ポリプロピレン製、 又はポリエステル製の板、 筒状、 シート、 不織布、 布、 繊維束等であることを特徴とする請求項 1又は 2記載の廃材の回収 方法。  5. The foam material is foamed polystyrene or foamed polyethylene, and the plastic container is a container made of polyethylene, polypropylene, or polyvinyl chloride, or a pet bottle, and the plastic material is 3. The method for recovering waste material according to claim 1, wherein the material is a plate, a tube, a sheet, a nonwoven fabric, a cloth, a fiber bundle, or the like made of polyvinyl chloride, polyethylene, polypropylene, or polyester. 6 . 前記溶液温度が 1 3 0 °C以上から沸点までの範囲内の温度であり、 前記廃 材が発泡スチロール、 ぺッ トボ トル又はポリ エチレン製の容器であるこ と を 特徴とする請求項 1又は 2記載の廃材の回収方法。  6. The solution according to claim 1, wherein the temperature of the solution is in a range from 130 ° C. or higher to a boiling point, and the waste material is a styrene foam, a pet bottle or a container made of polyethylene. Method of collecting waste materials described in 2. 7 . 前記プラスチック材が、 ペッ トボトルを粉砕又は細断して得られるチップ であることを特徴とする請求項 1又は 2記載の廃材の回収方法。  7. The method for collecting waste material according to claim 1, wherein the plastic material is a chip obtained by crushing or shredding a pet bottle. 8 . 前記発泡材が発泡ポリ ウレタンであり、 前記溶液温度が 1 5 0 °C以上から 沸点までであることを特徴とする請求項 1又は 2記載の廃材の回収方法。  8. The method for recovering waste material according to claim 1, wherein the foaming material is foamed polyurethane, and the solution temperature is from 150 ° C. or higher to a boiling point. 9 . 前記溶液が、 ポリ ウレタンの原料であるジオール又はト リオールであるこ とを特徴とする請求項 1又は 2記載の廃材の回収方法。 9. The solution is a diol or triol, a raw material for polyurethane. 3. The method for recovering waste materials according to claim 1, wherein: 1 0 . 前記ジオールがグリ コール類又はモノァシルグリ セ口ールであるこ と を 特徴とする請求項 1又は 2記載の廃材の回収方法。  10. The method according to claim 1, wherein the diol is glycols or monoacylglycerol. 1 1 . 前記ダリ コール類がアルキレンダリ コール類又はその重合体であること を特徴とする請求項 1 0記載の廃材の回収方法。  11. The method for recovering waste materials according to claim 10, wherein the dalicols are alkylenedaricols or a polymer thereof. 1 2 . 前記アルキレングリ コール類がジエチレングリ コール、 ト リ メチレング リ コール、 ト リエチレングリ コール、 テ トラエチレンダリ コール、 ブチレングリ コール、 ジプロピレングリ コール、 又は ト リ プロ ピレングリ コールであるこ と を 特徴とする請求項 1 1記載の廃材の回収方法。  12. The alkylene glycols are diethylene glycol, trimethylene glycol, triethylene glycol, tetraethylene dalichol, butylene glycol, dipropylene glycol, or tripropylene glycol. 11. The method for collecting waste material according to claim 11. 1 3 . 前記重合体が、 ポリエチレングリ コール又はポリ プロ ピレングリ コール であることを特徴とする請求項 1 1記載の廃材の回収方法。  13. The method according to claim 11, wherein the polymer is polyethylene glycol or polypropylene glycol. 1 4 . 前記ポリオールが ト リオールである請求項 1又は 2記載の廃材の回収方 法。  14. The method for recovering waste material according to claim 1, wherein the polyol is a triol. 1 5 . 前記トリオールがグリセリ ン、 又はトリ メチロールプロパンであること を特徴とする請求項 1 1記載の廃材の回収方法。  15. The method for collecting waste material according to claim 11, wherein the triol is glycerin or trimethylolpropane. 1 6 . 前記廃材がぺッ トボトル又はぺッ トボトルを破砕又は細断して得られるチ ップであり、 前記溶液がエチレングリ コールであることを特徴とする請求項 1又 は 2記載の廃材の回収方法。  16. The waste material according to claim 1, wherein the waste material is a bottle or a chip obtained by crushing or shredding a bottle, and the solution is ethylene glycol. Collection method. 1 7 . 前記ジオール又はポリオールを所定の温度に加熱する加熱装置と、 該加 熱された溶液と発泡材、 プラスチック容器、 又はプラスチック材とを接触させる 、 浸す、 かける、 吹き付けて減容 · 軟化させるための減容 · 軟化手段と、 該発泡 材、 プラスチック容器、 又はプラスチック材を収集する収集手段とを備える廃材 の回収装置。  17. A heating device for heating the diol or polyol to a predetermined temperature, and contacting, dipping, spraying, or spraying the heated solution with a foaming material, a plastic container, or a plastic material to reduce and soften the volume. A waste material recovery device comprising: a volume reducing / softening means for collecting the foamed material, a plastic container, or a collecting means for collecting the plastic material. 1 8 . 前記発泡材、 プラスチック容器、 又はプラスチック材に圧力を加えるため の加圧機をさらに備えることを特徴とする請求項 1 7記載の廃材の回収装置。 18. The waste material recovery device according to claim 17, further comprising a pressurizer for applying pressure to the foam material, the plastic container, or the plastic material. 1 9 . 前記加熱装置は、 誘導加熱装置、 マイクロ波加熱装置、 超音波加熱装置 、 高周波振動加熱装置、 又は超音波振動加熱装置のいずれか 1つ又は組み合わせ て構成されることを特徵とする請求項 1 7記載の廃材の回収装置。 2 19. The heating device is characterized in that it is configured by one or a combination of an induction heating device, a microwave heating device, an ultrasonic heating device, a high-frequency vibration heating device, and an ultrasonic vibration heating device. Item 17. A waste material recovery device according to Item 17. Two 2 0 . 前記廃材がぺッ トポトルであり、 その集合体より 1つが選別される手段 があり、 次に加温された液が加圧機底面より 自然落下、 吹きつけ、 スプレー等に よ り廃材と接触し、 ぺッ トボトルの少なく とも口部と底部の両方に圧縮力がかか る構造を備えることを特徴とする請求項 1 7記載の廃材の回収装置。 20. The waste material is a pot pottle, and there is a means to select one from the aggregate, and then the heated liquid is naturally dropped from the bottom of the press, sprayed, sprayed, etc. to remove the waste material. 18. The waste material recovery device according to claim 17, wherein a structure is provided in which at least both the mouth and the bottom of the pet bottle come into contact with each other and a compressive force is applied. 2 1 . タンクに減容液があり、 該タンクに廃材を入れて減容し、 又は減容しつ つある廃材を浮力によって液面に浮かせ、 減容した廃材を斜め上方に上昇するべ ル トによ り掬い上げる構造を備えることを特徴とする請求項 1 7記載の処理装置 2 1. There is a volume reduction liquid in the tank, and the waste material is put into the tank to reduce the volume, or the waste material whose volume is decreasing is floated on the liquid surface by buoyancy, and the reduced volume waste material is lifted diagonally upward. 18. The processing apparatus according to claim 17, wherein the processing apparatus is provided with a structure for scooping. 2 2 . ジオール又はポリオール溶液もしく はそれらの混合液からなり、 8 0 以上 2 0 0 °C以下に加熱した発泡材、 プラスチック材、 又はプラスチック容器の 減容又は軟化液。 22. A volume-reducing or softening liquid made of a diol or polyol solution or a mixture thereof and heated to a temperature of 80 to 200 ° C and below. 2 3 . ジオール又はポリオール溶液もしく はそれらの混合液からなり、 1 3 0 °C 以上 2 0 0 °C以下に加熱した発泡スチロール又はポリエチレン製品の減容又は軟 化液。  23. A volume reduction or softening solution of styrofoam or polyethylene products consisting of a diol or polyol solution or a mixture thereof and heated to 130 ° C or more and 200 ° C or less. 2 4 . 溶液がポリ ウレタ ンの原料となるジオール又はト リオールであり、 1 5 0 °C以上 2 3 0 °C以下に加熱した発泡ポリ ウレタンの減容又は軟化液。  24. A volume reducing or softening solution of foamed polyurethane heated to a temperature of 150 ° C or higher and 230 ° C or lower, wherein the solution is a diol or a triol as a raw material of the polyurethane. 2 5 . 溶液がエチレングリ コールであり、 8 0 °C以上 1 9 0 °C以下に加熱した ぺッ トボトル又はそのチップの減容又は軟化液。 25. A volume-reduced or softened solution of a bottle or its tip heated to a temperature of 80 ° C or more and 190 ° C or less, wherein the solution is ethylene glycol. 2 3 . 請求項 1又は 2項記載の廃材の回収方法によ り回収した廃プラスチック 部材の重量に応じて引き取り価格が決められる廃材の回収システム。  23. A waste material recovery system in which the collection price is determined according to the weight of the waste plastic member recovered by the waste material recovery method according to claim 1 or 2. 2 4 . 請求項 1又は 2項記載の廃材の回収方法によ り回収した発泡スチロール を必要に応じて水洗し、 又は乾燥して、 減圧式の成形機によりスチロール製品を 得る発泡スチロールのリサイクル方法。 24. A method for recycling styrofoam, wherein the styrofoam collected by the method for collecting waste material according to claim 1 or 2 is washed or dried as necessary to obtain a styrene product by a reduced-pressure molding machine. 2 5 . ジオール又はポリオールと廃材とを混合し、 液面にあるものと、 液中又 は底に沈むものに分けた後、 それぞれを回収するプラスチックの廃材の分別回収 方法。  25. A method of separating and collecting plastic waste materials by mixing diols or polyols and waste materials, separating them into those that are on the liquid surface and those that sink in the liquid or at the bottom, and then recovering each.
PCT/JP2003/014127 2002-11-12 2003-11-06 Waste collecting method, waste collecting apparatus, volume reducing or softening solution, waste collecting system, waste recycling method, and classified waste collecting method Ceased WO2004044042A1 (en)

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