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WO2000045994A1 - Grinding beads and beads production method and device therefor - Google Patents

Grinding beads and beads production method and device therefor Download PDF

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Publication number
WO2000045994A1
WO2000045994A1 PCT/JP2000/000516 JP0000516W WO0045994A1 WO 2000045994 A1 WO2000045994 A1 WO 2000045994A1 JP 0000516 W JP0000516 W JP 0000516W WO 0045994 A1 WO0045994 A1 WO 0045994A1
Authority
WO
WIPO (PCT)
Prior art keywords
crushing
beads
crushed
resin
molded product
Prior art date
Application number
PCT/JP2000/000516
Other languages
French (fr)
Japanese (ja)
Inventor
Naoyoshi Tomioka
Original Assignee
Bridgestone Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Bridgestone Corporation filed Critical Bridgestone Corporation
Priority to AU23234/00A priority Critical patent/AU2323400A/en
Priority to JP2000597095A priority patent/JP3626098B2/en
Publication of WO2000045994A1 publication Critical patent/WO2000045994A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C4/00Crushing or disintegrating by roller mills
    • B02C4/02Crushing or disintegrating by roller mills with two or more rollers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C23/00Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
    • B02C23/08Separating or sorting of material, associated with crushing or disintegrating
    • B02C23/10Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone

Definitions

  • the present invention is applicable to the grinding of various metal and synthetic resin parts, the peeling of coating films, rust, burrs, adhesive layers, seals, etc., the cleaning and polishing of various tools, jigs, polishing, road marking signs or concrete.
  • the present invention relates to beads used for instantaneous peeling of wall stains and the like, and further relates to a method and an apparatus for producing the beads.
  • thermosetting resin Fine beads of thermosetting resin are sprayed by air pressure to grind the surface of various metals, synthetic resins-wood, glass, and other materials, and paint films, rust, burrs, adhesive layers, seals, and waxes.
  • a method of instantaneously peeling off road markings, dirt, graffiti, etc. on road surface signs, concrete wall surfaces or tiles such as white roads For example, in Japanese Patent Application Laid-Open No. HEI 4-111776, a molded product obtained by adding a filler such as a reinforcing material or a filler, a coloring agent, or the like to a thermosetting resin, kneading the mixture, and heat-curing to cure the molded product is used.
  • the powder is crushed into a mesh of 5 to 100 to provide an abrasive for a base treatment of a coating, and this is sprayed onto a coating surface of a metal product to peel off the coating.
  • a thermosetting resin is cured and pulverized, treated with a titanium coupling agent, and dispersed in the thermosetting resin before curing. It discloses that the material is ground into an abrasive.
  • Japanese Patent Application Laid-Open No. H8-733813 in order to eliminate the electrification on the object to be cleaned by the resin particles for cleaning, the electric potential elimination of the ether 'nitrile compound is applied to the resin particles for cleaning.
  • Thermosetting resins have long been manufactured and sold as fine powder dried resins and resins for granular molded products.
  • Melamine resin and Urea resin as raw materials (raw materials) It is standardized as a general-purpose product with specific gravity, hardness, etc. (JIS K 6917, K 6916), with 60 to 70% of melamin powder and 2 to 4 monograms per melamin monolayer. (30% to 40% aqueous solution of formaldehyde), 0.1% catalyst, and 40% to 30% filler such as pulp Molded melamine resin has a hard surface and no filling It is also known that the specific gravity in the case of lumber: 1.48 rises to some extent.
  • thermosetting resin molded products with a circular or polygonal cross section are obtained by cutting thermosetting resin molded products with a circular or polygonal cross section into fine pieces in the shape of a cylinder or a square tube.
  • the peeling ability was insufficient, and it took time to completely peel off, and there was a limit to the particle size adjustment.
  • a first object of the present invention is to provide a pulverized thermosetting resin molded product, in which each particle is formed into an irregularly shaped polyhedral fine substance substantially surrounded by a sharp ridgeline, and a particle size at a classification stage.
  • An object is to provide beads that are almost homogenized within a certain range.
  • a second object of the present invention is to roughly pulverize a plate-like molded product of a thermosetting resin, and then pulverize between rolls having irregularities with a phase difference of 1/2 pitch formed on the roll surface. Accordingly, it is an object of the present invention to provide a method and an apparatus for producing beads for grinding and peeling an irregular polyhedron having a sharp ridge line. Disclosure of the invention
  • the beads according to the present invention are characterized by having the following configuration.
  • the present invention relates to a crushed product of a thermosetting resin molded product having a particle size of 1000 to about 5.0 m, wherein each particle is substantially irregular and fine polyhedron surrounded by sharp ridges. This is a grinding / peeling bead whose grain size at each classification stage is almost homogenized within a certain range.
  • the thermosetting resin is filled with pulp and glass fiber crushed pieces, and further contains carbon, artificial graphite or metal fibers. Specifically, 30 to 40% of a valve and 0.1 to 0.5% of a glass fiber cloth piece are mixed in the thermosetting resin material after condensation, and static electricity is generated after the resin is aged and dried. Compounded with carbon powder or artificial graphite with electrical conductivity of 0.2 to 0.3 for suppression and electrification suppression, and 0.1 to 0.5% of metal powder or metal fiber to increase specific gravity to 1.8 or more I do.
  • the present invention uses a thermosetting resin plate-like molded product.
  • the obtained product is crushed (roughly divided) into a die shape or a pellet shape, and then the irregularities on the roll surface facing the same are obtained. Is crushed by a multi-stage crushing roll arranged with a 1/2 pitch phase shift to form irregular polyhedral fines (beads) with sharp ridges.
  • thermosetting resin melamine resin (melamine-formaldehyde resin), urine resin (urea-formaldehyde resin), phenol resin, and unsaturated resin Polyester, acrylic, guanamine, epoxy or polyurethane alone, or with hardness and specific gravity ⁇
  • thermosetting resins with different viscosities can be mixed. These materials are non-polluting even when used, have high electrical insulation resistance for the purpose of expanding the range of use, are resistant to alkaline acids, are relatively high in heat resistance, Non-flammable (flammable, ignitable), non-toxic (styrene, ester, etc.), and relatively powdery due to the impact of nozzle injection during recycling.
  • a force for crushing a resin plate-like molded product obtained by mixing a urea resin and / or a phenol resin with a melamine resin, or a melamine resin, a urea resin, or a phenol resin
  • the different types of resin plates are coarsely crushed and mixed, and then ground to form irregular polyhedral fines.
  • a plate-shaped molded product of thermosetting resin is an irregular shape of approximately 2 to 4 mm square (maximum thickness 5 mm, flat object with approximately 7 sides).
  • a crusher section that crushes into a shape like a pellet, a sorting section that removes metal and foreign matter in crushed material crushed by a part of the crusher, and a 1Z2 pitch Coarse with crushing rolls for crushing the crushed material selected at the sorting unit with irregularities formed with a phase shift Similar to the crushing part of the crushing part and the crushing part, there is also a phase shift of 1 Z 2 pitch on the roll surface.
  • the crushed material obtained in the crushing part with irregularities formed has a particle size of 100 to 500 ⁇ m. It comprises: a crushing section having a multi-stage crushing roll pair for processing into amorphous fine polyhedral beads having a sharp ridge at ⁇ ; and a classification device arranged downstream of the crushing section.
  • the crushing unit equipped with the above-mentioned multi-stage crushing roll pair has a particle size adjustment mechanism that changes and adjusts the bead particle size by setting the unevenness pitch of the crushing rolls and the clearness between the opposing rolls to be optimal. I have it.
  • this bead manufacturing apparatus arranges a classifier such as an air classifier, an electric power classifier, and a vibrating sieving machine downstream of the pulverizing section to classify the beads, weigh and classify the classified beads.
  • a classifier such as an air classifier, an electric power classifier, and a vibrating sieving machine downstream of the pulverizing section to classify the beads, weigh and classify the classified beads.
  • a circulation line is provided to return the fines above or below the mesh in each classifying step upstream of the sorting section or upstream of the crushing section, and the fine particles generated in each step from the crusher section to the classifying apparatus are provided. Equipped with a powder transport conveyor or duct that guides dust containing particles to the dust treatment equipment.
  • a vibrating sieve having several stages of sieves with successively finer stitches and deriving shoots from sieves on each sieve is suitable.
  • the first-stage mesh-up is sent to the crusher and crushed again, and the lower-most mesh under is discarded as dust.
  • the beads obtained by the present invention can be ground without damaging various metals, synthetic resins, wood, glass and other products, or painted films, adhesive layers, seals, waxes, concrete walls or tiles. Used for instantaneous peeling of stains and graffiti.
  • the products to be processed include coating and peeling of equipment and parts, rust removal, reproduction of defective coating, electrical components, molded products, molds, cleaning of jigs, etc. It is used for polishing, polishing, road marking (white line, etc.), and peeling off of adhering materials or seals on buildings.
  • the advantages of using the above bead are that the speed of grinding and peeling has been shortened, making it possible to shorten the working time, not to damage the work, to reduce costs, and to reduce dust and dust. Low noise generation.
  • the beads of the present invention are excellent in antistatic properties, economical efficiency and grinding / peeling properties, and are suitable for recyclability, as described below. 1.
  • a specific filler is blended to form a peeling bead. The aim is to improve the effect of removing particles.
  • Carbon powder (carbon black) is blended as filler (trace%).
  • Molding of resin plate The above-mentioned raw material is filled in a mold, and molded (Zmra for 60 to 180 seconds) under pressure (150 to 200 kg / cm 2 ) and heating (130 to 165 ° C).
  • the molding time varies depending on the thickness of the molded product, but a high hardness can be obtained by increasing the molding time at a low temperature.
  • High-end products such as resin products, electronic components or molded products
  • FIG. 1 is a flowchart of the method for producing a peeling bead of the present invention.
  • FIG. 2 is a layout diagram showing an outline of a bead manufacturing apparatus for carrying out the present invention.
  • FIG. 3 is a perspective view of the crushing unit of FIG.
  • FIG. 4 is an enlarged perspective view of the grinding roll pair in FIG.
  • FIG. 5 is an enlarged cross-sectional view of the uneven teeth of the crushing roll.
  • FIG. 6 is an enlarged sectional view showing the deformation of the uneven teeth of the crushing roll.
  • FIG. 7 is a layout diagram showing details of each part from pulverization to packaging in FIG.
  • FIG. 8 is an enlarged plan view illustrating a group of peeling beads.
  • Figure 1 shows the bead production flow
  • Melamine powder 1a, formalin 1b, and alcohol or acid catalyst 1c are charged into reaction tank 2 and polymerized and condensed, and then transferred to mixing tank 3 to be used as a filler.
  • carbon powder (a carbon black having a conductivity of 0.3%) for suppressing static electricity generation during blasting and a carbon powder for increasing the specific gravity are used.
  • 0.1 to 0.5% of metal fiber 6a is blended, and a coloring material is blended if necessary.
  • molding material (melamine resin) 8a obtained by almost the same procedure as above, knead 8c, pressurize and heat and mold to form a resin with a thickness of 2 to 5 mm with different hardness and specific gravity Get 10
  • the raw material is formed into a plate-like material, and the process from crushing (crushing) to crushing and packaging is not only performed consistently, but it is divided into several processes.
  • a crusher 11 for crushing each of the above-mentioned plates 10 into a die or a pellet of about 2 to 4 mm square, a pre-mixing section 12 for mixing crushed materials, and a magnetic separation for foreign substances. Separation section 14, crushing 15, crushing with several crushing rolls 16, sieving 18, weighing 23, packing 24, and then unloaded 25.
  • FIG. 2 is a front view schematically showing a bead manufacturing apparatus
  • FIG. 3 is an enlarged perspective view of a crushing unit in FIG. 2
  • FIG. 4 is an enlarged cross-sectional view of a crushing roll in FIG.
  • the resin plate 10 is selected from molding materials such as melamine resin, urea resin, phenol resin, unsaturated polyester, acrylate, guanamine, epoxy or polyurethane. 60% to 80% of melamine mixed with 40% to 20% of urea, one resin is made of melamine, urea, and funinol resin. It may be a mixture of two or more types of mixed materials, such as mixing.
  • the melamine resin plate and the urea resin plate or the phenol resin plate may be crushed by a crusher, and then mixed. Unlike conventional hammer mills, disk crushers, cone crushers, oscillators, etc., the crusher 11 has several movable blades (closed flat cutters with serrated blades) attached to the rotor.
  • a type that crushes between the fixed blade and the fixed blade by rotation of the rotor (not shown) is used.
  • Hammer type crushers are not effective because only a lot of cracks appear in the crushed product or dust is generated during crushing.
  • the resin plate 1 ⁇ is not limited to sheet-like material, but should be used in advance to crush crushed thermosetting resin materials, such as sprues, runners and defective moldings generated during molding of resin materials.
  • the crusher unit 11 in Fig. 2 is omitted and the mixture is directly introduced into the mixing unit 12. You may. [Crushing and sieving of crushed material]
  • An automatic feeder 13 and a rectifying feeder 13a are provided below the mixing section 12.
  • the crushed material flowing down by the rectifying feeder 13a is rectified into a layer having a substantially uniform thickness, and sent to the metal ⁇ 'sorter 14 for removing foreign matter.
  • a crushing unit (with a pair of crushing rolls and a static eliminator) 15 and a crushing unit (multi-stage crushing roller pair and a static eliminator) 16 are provided, and further switched It is connected to a screening section 18 through a valve 17.
  • the sieving section 18 is composed of an air classifier 21 for classifying fine particles and a power classifier 22 for classifying large-diameter particles from fine particles.
  • the classified granules (beads for peeling) are packaged into peeling beads of a predetermined volume by the bagging machine 23 with an automatic weighing machine, which corresponds to the packaging shipping department, and the automatic bag mouth sewing machine 23, and the transporter 2 It is carried out of the site using 5 mag.
  • the fines on the mesh of the electric power classifier 22 are introduced into the circulation pipe 26a and returned to the rectifier feeder 13a with hopper upstream of the sorting section 14a.
  • the fine particles on the mesh of 21 are introduced into the circulation pipe 26 b and returned upstream of the crushing section 15.
  • the dust generated at each stage is sent to an upper dust treatment device (separation device) 28 through a duct 27 as shown by the dotted line in Fig. 2, and the dust having a predetermined particle size is passed to the mixer 12.
  • the fine powder having a predetermined particle size or less is sent to the dust collector 29 for disposal.
  • 15a and 15a are crushing rolls
  • 15b is a honno
  • 15c is a rectifying feeder for rectifying the crushed material flowing down from the hobber into a layer having a substantially uniform thickness.
  • the crushing roll 15a has lateral grooves 35 extending in the generatrix direction at regular intervals on the circumference of the roll surface, as described later for the crushing roll, and has many irregularities 36 on the roll surface. Let me.
  • crushed pieces of 2 to 4 mm square die or pellets at the crusher section 11 are crushed into approximately 2 mm square by rotating the crushing rolls 15a and 15a. I do.
  • FIG. 3 is an enlarged perspective view of the crushing section 16 in the bead manufacturing apparatus
  • FIG. 4 is a perspective view of a crushing roll pair.
  • a pair of pulverizing rolls 31, 31, 32, 32, 33, and 33 are laid on the frame 30 in three vertical stages.
  • Each roll surface has several (four) lateral grooves 35 extending in the generatrix direction at regular intervals on the circumference, and a number of mountain-shaped irregularities 36 on the roll surface.
  • Fig. 5 Ni will Yo described later, the mouth one by operating the Lee Nde' click scan gauge dial 3 7. Le gap 0.1 to adjust to 0. 2 m m ( Figure 4).
  • Figure 6 shows a roll with a number of angular irregularities 36a formed on the roll surface.
  • a scraper 38 is placed close to each roll.
  • 40 is a motor with a speed reducer
  • 41, 42, and 43 are portal shafts of each stage
  • 44 is a chain hung between the motor and the first stage roll shaft sprocket
  • 45 is a chain hung between the sprockets of the roll rollers facing each other.
  • a synchronous rotation gear (not shown) is interposed between the opposing first-stage roll shafts.
  • the roll pitch is gradually increased while the roll pitch is gradually reduced from the first stage to the third stage.
  • the diameter of each roll is 150 mra, and the uneven pitch and rotation speed of each stage are as follows.
  • the rolls of the crushing section 15 also have the same irregularities.
  • the end of the top is abutted against the side wall of the frame to form the alignment mechanism. Adjusting the effective length of the adjust port by manual operation, and slightly moving the rear roll in the axial direction, aligning the roll unevenness (peaks and valleys). Is achieved.
  • the clearance between the rolls is adjusted according to the hardness, material, grain size, etc. of the resin, but is usually about 0.11 to 0.3 mm or more.
  • Adjusted to the left and right bearings of the other roll (for example, the roll 31 in front of each stage in Fig. 2) supported to be movable in the front-rear direction Screw 37a is fixedly attached, and index handles (index gauge dials) 37, 37 are provided at the ends thereof.
  • Adjustment of the clearance is performed by rotating the index handle and moving the left or right or left or right bearing in the front-rear direction.
  • FIG. 3 only the index handles 37 and 37 on the right side of the frame are shown, and the index handle on the left side is not shown.
  • the homogenization is performed using special rolls of several stages in the crushing and crushing sections.
  • the roll shape pitch, clearance
  • a static electricity eliminator is installed in the crushing section and crushing section to prevent static electricity from being generated in places (sites) where pressure, impact, shear, and friction occur on the material.
  • Dust containing fine particles generated at each stage from the crusher section to the classifier can be extracted from, for example, Patent No. 2891 163 1 (Japanese Patent Application Laid-Open No. Hei 8-252223).
  • the particles are separated into reusable granular beads and dust by a granular separation device (dust treatment device) as disclosed in (1).
  • the granular material separation device includes: a cylindrical separation container (separation chamber); a storage container formed on the outer periphery of the separation container; dust and renewable fine particles generated during the crushing step. (Beads) are blown into the separation container (2) together with compressed air, so that a carry-in tube is attached to the separation container through the side wall of the storage container; and is arranged in the separation container and is delivered from the carry-in tube.
  • a diffusion member for diffusing and separating the dust and renewable beads obtained by the difference in mass comprising a group of discs with punching holes or slits which are spaced apart from each other and stacked in several stages;
  • a discharge pipe for dust provided on a side wall near the top of the containment vessel; and a tank disposed below the containment vessel and the separation vessel to accommodate renewable beads after dust separation. Is composed of I have.
  • the separation container discharges dust that has not passed through the diffusion member to a discharge pipe near the top of the storage container, and is higher than a bead receiving surface of the diffusion member.
  • the storage container is further provided with a first discharge port, and the storage container is configured to discharge dust floating through the punching holes or slits of the diffusion member into the reusable bead storage tank and floating to the discharge pipe side.
  • a second outlet is provided at the bottom of the containment tank, which is the upper plate of the storage tank.
  • the reusable beads and dust are extremely efficiently diffused by the diffusion member composed of a plurality of upper and lower punching holes or a group of disks with slits arranged in the separation container.
  • the diffusion member composed of a plurality of upper and lower punching holes or a group of disks with slits arranged in the separation container.
  • the details of the particle separation device (dust treatment device) 28 are omitted from the drawings because they are disclosed in the aforementioned Japanese Patent No. 2891631, but the mixture of reusable beads and dust generated at each stage is suctioned. It is transported into the separation vessel (separation chamber) by duct 27. Since the dust collector 29 is operating, the inside of the separation vessel is under negative pressure. Therefore, the mixture of beads and dust blown from the inlet violently collides with the inner wall of the separation container, the lower surface of the inner lid, and the upper surface of the uppermost diffusion plate and diffuses at high speed.
  • the reusable particles having a large mass and the dust not discharged from the first discharge port 46 pass through the respective punch holes or slits of the diffusion plate (not shown) and pass onto the diffusion plate. It falls and collides with the upper surface of the diffuser plate to diffuse.
  • the low-mass dust is again blown up, and is discharged from the first discharge port 46 through each punch hole or slit of the diffusion plate.
  • the reusable particles and the remaining small amount of dust that have passed through the diffusion plate fall down to the lower part of the hopper tank. (2) It is blown out from the discharge port (47) and discharged from the dust discharge port through the space between the outer wall and the inner wall of the separation container (28).
  • This section describes the reuse of beads during blasting.
  • the beads By spraying on the target object, the beads are crushed to reduce the particle size, and the sharp ridge portion is rounded.
  • the beads are repeatedly reused by sieving using the separation device. Even if the bead diameter becomes smaller, the polyhedral shape of each particle and the grinding / peeling efficiency do not change.
  • Target It can be reused several to several tens times (for example, 60 times) depending on the hardness of the product, the hardness of the beads, specific gravity, air pressure, spray angle, spray distance, etc.
  • MG-14 (106 ⁇ m or less, for example, about 50 ⁇ m) does not recycle only once.
  • the first discharge port 46 is arranged to face the upper surface of the diffusion plate, which is the particle receiving surface of the diffusion member. Therefore, the dust diffused by the diffusion member can be easily blown out.
  • the first discharge port 46 is disposed above the upper surface of the diffusion plate, which is the particle receiving surface of the diffusion member. Therefore, the possibility that the reusable beads having a large mass are blown out from the first outlet 46 is reduced, and as a result, the separation accuracy is improved.
  • a second discharge port 47 is provided above the hobba, which is a reusable granule storage tank. Accordingly, the possibility that the reusable granules having a large mass are blown out from the second discharge port 47 is reduced.
  • FIG. 7 is an arrangement diagram of each device showing another example from crushing to packaging.
  • the beads crushed by the roll crusher 16 shown in FIGS. 2 and 3 are classified by the vibrating sieve 20.
  • This vibrating sieve 20 has several stages of sieve nets 50 to 53 (for example, 6, 20, 32, 50 meshes) in which the stitches are sequentially made fine, and hits each sieve net.
  • the shoots 50a to 53a from the outer wall of the sieve and the shoots 54 from the bottom of the lowermost sieve are led out and connected to the conveyor or ducts 55 to 59, respectively.
  • Each sieve mesh 50 to 53 provided inside the vibrating sieve 20 can be replaced with any mesh, and the bead size is classified within the range from 10 mesh or less to 150 mesh. It is possible to do so.
  • the crusher 16 and the sieving machine 20 in FIG. 7 can be installed in two or more lines, but for simplicity of explanation, the case where only one line is used is illustrated and described.
  • the first bagging line 60 is provided by a switching damper 61 provided at the downstream end of the conveyor 57, and is provided with a double-toned flexible container (flexible container) filling machine 62 and a 20 kg bagging machine 62. Connected to 0.
  • the frecon packing machine 62 consists of a hopper with a level detector 63, a loading dang, ° 64, a frecon bag 65, a platform scale 66 and a conveyor 67, and a 20 kg bag filling machine
  • Reference numeral 70 denotes a hopper 71 with a level detector, a hopper 72 with a weighing and sewing machine, a bag 74 and belt conveyors 75, 76.
  • the second bag-filling line 80 is a hopper 81 with a level detector, a screw conveyor 82, an input dumper 83, and a hood 81 with a level detector provided at the lowermost end of the powder transport conveyor 58. It consists of a phono with a measuring device, ° 84, and 20 kg packaging bags 86 are sequentially carried out by a conveyor.
  • beads made of thermosetting resin such as those described above are mixed.
  • These beads 90 have a hardness (Mohs) of 3.0-4.5, specific gravity 1.:! ⁇ 1.52, size 10 ⁇ : L50 mesh (about 10000 ⁇ : ⁇ ⁇ ⁇ ) ⁇ ), as shown in Fig. 8 (25 times), each forms an irregular polyhedron with sharp edges. However, it can be used even if it is 100 ⁇ m or less (for example, 50 ⁇ m).
  • beads ejection amount is 1.
  • the peel time per m 2 is 3 to 6 mi m 2 .
  • the number of recycles of beads depends on the pressure, but is usually 15 to 40 or more.
  • the performance of the above beads is primarily specified by material, hardness and specific gravity, secondary is excellent in cutting performance, abrasion resistance, heat resistance, anti-static property, and tertiary is blast
  • the work speed is high, the dust generation rate is low, the reusability is high, and the bead dust itself is pollution-free and can be treated as general waste.
  • MG-0 for peeling bumper chips
  • MG-1 for coating hard materials (steel materials) for removing oxide scale and road markings
  • MG-1 for coating films, rust, Paris, adhesives, seals, floor wax, etc.
  • MG-3 or MG-15 for cleaning of peeling, anti-glare on metallic glossy surfaces, walls or tiles, coating film of soft material (such as aluminum) 'Rust' Burr.
  • MG_7, soft for wall cleaning MG-10 or MG-14 is used for wall coating or floor cleaning.
  • a 3 to 5 mm thick plastic plate-like molded product formed by heating and pressing a mixed material of 6% by weight of melamine resin and 40% of urea resin by a crusher. After being crushed into a batter shape, it was roughly crushed and pulverized by the above-mentioned device to obtain a release material of 20 to 65 mesh, which was sprayed on an aluminum can coating film to peel off the coating film.
  • the capacity of one 6 mm diameter nozzle is 2 kgcm 2 air pressure and the amount of beads ejected is 1.
  • a mixture of 70% of crushed resin plate and 30% of crushed resin plate was crushed by a crusher, and then crushed and pulverized.
  • As a release material for 0 to 65 mesh, the coating film was peeled off by spraying it onto the aluminum can coating film, and the coating film was successfully removed as before.
  • a crushed plate-like resin molded product molded from a mixed material of a melamine resin and a phenol resin is crushed and crushed by the above-mentioned equipment to obtain a mesh release material of 20 to 65, which is used as a steel can.
  • the coating film was peeled off by spraying on the 100 micron coating film. 6 mm ⁇ No capacity per one nozzle is, the air pressure 3 kg / cm 2, a bead ejection amount 1. O kg Zmin, 1 m 2 per stripping time 3 result treated with MinZm 2, and cleanly peeled coating film A metallic luster could be exhibited.
  • the present invention is characterized in that in the production process, after crushing in a crushing section, crushing and sieving are performed by several stages of crushing rolls, so that the crushing is performed at each classification step adapted to the purpose of work processing. Grinding or peeling beads with a uniform particle size can be easily manufactured. In particular, emphasis is placed on the shape of the crushing roll (concavo-convex pitch, clearance of the opposing roll), and grinding and polishing of various workpieces. In addition, irregular polyhedral beads suitable for instantaneous peeling can be provided. By selecting the shape of the crushing roll, it is easy to change and adjust the bead particle size, and it is possible to efficiently produce beads with less generation of dust and noise during the crushing process.
  • the homogenization of the particle size of the beads improves the grinding and peeling ability, and can shorten the work time for instantaneous peeling and the like. Furthermore, beads that are useful for peeling work such as peeling off coatings on aluminum cans, steel cans, automobile bumpers, etc., and regenerating non-consumables can be efficiently used without damaging the peeled product (work). It can be manufactured.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

Grinding or separating beads which are easy to adjust in grain size, consist of amorphous polyhedral slender elements suitable for instantaneous separation, and have classification-based homogeneous grain sizes. The beads production device comprising crusher units (11) for roughly crushing platy moldings of thermosetting resin into a dice- or pellet-form and a roll-type crushing unit (16). The crushing unit (16) comprises multi-stage crushing rolls (31 to 33) in which irregularities (36) formed on the surfaces of each pair of facing rolls are phase-deviated at 1/2 of a pitch and which crushes coarsely-crushed thermosetting-resin pieces into specified sizes. Classifying devices (20, 21, 22) disposed downstream the crushing unit (16) classify the resultant pieces to provide beads which are homogenized according to classification and which consist of amorphous polyhedral slender elements having sharp ridges.

Description

明 細  Details
研削用ビーズと ビーズの製造方法並びに製造装置 Grinding beads and method and apparatus for producing beads
技術分野 Technical field
本発明は、 各種金属 · 合成樹脂製部品等の研削、 塗装膜 · サビ , バリ · 接着剤 層 . シールなどの剥離や、 各種工具 ' ジグの洗浄 . 研磨、 道路面標示標識又はコ ンク リー ト壁面汚れなどの瞬間剥離に用いるビーズにかかるものであり、 更にそ のビーズの製造方法並びに製造装置に関する。  The present invention is applicable to the grinding of various metal and synthetic resin parts, the peeling of coating films, rust, burrs, adhesive layers, seals, etc., the cleaning and polishing of various tools, jigs, polishing, road marking signs or concrete. The present invention relates to beads used for instantaneous peeling of wall stains and the like, and further relates to a method and an apparatus for producing the beads.
背景技術 Background art
熱硬化性樹脂の微細なビーズを、 空気圧によ り吹き付けて各種金属 ·合成樹脂 - 木材 · ガラスなどの素材表面の研削や、 塗装膜 · サビ ' バリ ·接着剤層 · シール · ワ ッ ク スの剥離、 或いは道路白線等の路面標識 · コ ンク リー ト壁面又はタイ ルの 汚れ、 落書きなどを瞬間剥離する方法が知られている。 例えば、 特開平 4 一 1 0 1 7 7 6号では、 熱硬化性樹脂に補強材、 充填材等のフ ィ ラーや着色剤等を添加 混練し、 加熱成形して硬化させた成形物を粒度 5〜 1 0 0 メ ッシュに粉砕して塗 装の下地処理用研磨材と し、 これを金属製品の塗装面に吹き付けて塗膜を剥離す るこ とを開示している。 特開昭 6 1 — 1 5 2 3 7 0号では、 熱硬化性樹脂を硬化 粉砕した微粒子をチタンカ ップリ ング剤で処理し、 これを硬化前の熱硬化性樹脂 に分散させた後、 硬化、 粉砕して研磨材とするこ とを開示している。 また、 特開 平 8 — 7 3 8 1 3号では、 研掃用樹脂粒に研掃対象物での帯電を消去するため、 研掃用樹脂粒にエーテル ' 二 ト リル系化合物からなる電位消去材を配合してブラ ス 卜研削やバ レル加工に使用される研掃材について開示している。 更に、 特開平 8 - 9 0 4 2 0号では、 熱硬化性樹脂の粗粉砕後又は微粉砕後に粉砕品を熱処理 するこ とによ り 、 樹脂粒研磨材の硬度の均一化、 衝撃破壊強度の向上、 含水率の 均一化をはかった研磨材について開示している。  Fine beads of thermosetting resin are sprayed by air pressure to grind the surface of various metals, synthetic resins-wood, glass, and other materials, and paint films, rust, burrs, adhesive layers, seals, and waxes. There is known a method of instantaneously peeling off road markings, dirt, graffiti, etc. on road surface signs, concrete wall surfaces or tiles such as white roads. For example, in Japanese Patent Application Laid-Open No. HEI 4-111776, a molded product obtained by adding a filler such as a reinforcing material or a filler, a coloring agent, or the like to a thermosetting resin, kneading the mixture, and heat-curing to cure the molded product is used. It discloses that the powder is crushed into a mesh of 5 to 100 to provide an abrasive for a base treatment of a coating, and this is sprayed onto a coating surface of a metal product to peel off the coating. In Japanese Patent Application Laid-Open No. 61-152,370, a thermosetting resin is cured and pulverized, treated with a titanium coupling agent, and dispersed in the thermosetting resin before curing. It discloses that the material is ground into an abrasive. Also, in Japanese Patent Application Laid-Open No. H8-733813, in order to eliminate the electrification on the object to be cleaned by the resin particles for cleaning, the electric potential elimination of the ether 'nitrile compound is applied to the resin particles for cleaning. It discloses abrasive materials used for blast grinding and barrel processing. Further, in Japanese Patent Application Laid-Open No. 8-90420, heat treatment of a pulverized product after coarse pulverization or fine pulverization of a thermosetting resin is carried out, whereby the hardness of the resin abrasive particles is made uniform, and the impact fracture strength is improved. Abrasives with improved water content and uniform moisture content are disclosed.
熱硬化性樹脂は、 微粉末乾燥樹脂及び粒状成形品用樹脂と して古く から製造さ れ、 販売されている。 素原料 (素資材) と してのメ ラ ミ ン樹脂、 ユリ ア樹脂は、 汎用品と して比重、 硬度など規格化され (J I S K 6917 , 同 K 6916 ) ており、 メ ラ ミ ンノ ウダ一 6 0〜 7 0 %、 メ ラ ミ ン 1 モノレに 2〜 4 モノレのホルマ リ ン (ホルム ァルデヒ ドの 3 0〜 4 0 %水溶液) 、 触媒 0 . 1 %、 パルプなどの充填材 4 0〜 3 0 %を用いて成形したメ ラ ミ ン樹脂は、 表面が硬く 、 無充填材の場合の比重 : 1 . 4 8前後のものがある程度上昇するこ と も知られている。 Thermosetting resins have long been manufactured and sold as fine powder dried resins and resins for granular molded products. Melamine resin and Urea resin as raw materials (raw materials) It is standardized as a general-purpose product with specific gravity, hardness, etc. (JIS K 6917, K 6916), with 60 to 70% of melamin powder and 2 to 4 monograms per melamin monolayer. (30% to 40% aqueous solution of formaldehyde), 0.1% catalyst, and 40% to 30% filler such as pulp Molded melamine resin has a hard surface and no filling It is also known that the specific gravity in the case of lumber: 1.48 rises to some extent.
従来の剥離材、 研削材または研掃材は、 断面円形又は多角形の細線状の熱硬化 性樹脂成形物を切断して円筒または角筒状の微細片と したものであるから、 対象 物 (ワーク) に吹き付けたときに剥離能力が不十分で、 完全剥離までに時間を要 するも のであり 、 また粒度調整に限界があった。  Conventional release materials, abrasive materials or abrasive materials are obtained by cutting thermosetting resin molded products with a circular or polygonal cross section into fine pieces in the shape of a cylinder or a square tube. However, when sprayed onto a workpiece, the peeling ability was insufficient, and it took time to completely peel off, and there was a limit to the particle size adjustment.
そこで、 本発明の第 1 の目的は、 熱硬化性樹脂成形物の粉砕物で、 各粒子が実 質的に鋭利な稜線で囲まれた不定形な多面体微細物と され、 かつ分級段階の粒度 がある範囲内にほぼ均質化されている ビーズを提供するこ とにある。 さ らに、 本 発明の第 2の目的は、 熱硬化性樹脂のプレー 卜状成形物を粗砕したのち、 ロール 表面に 1 Ζ 2 ピッチ位相ズレした凹凸を形成したロール間で粉砕するこ とによ り、 鋭利な稜線を持つ不定形な多面体の研削 · 剥離用ビーズを製造する方法、 装置を 提供するこ とを目的とする。 発明の開示  Therefore, a first object of the present invention is to provide a pulverized thermosetting resin molded product, in which each particle is formed into an irregularly shaped polyhedral fine substance substantially surrounded by a sharp ridgeline, and a particle size at a classification stage. An object is to provide beads that are almost homogenized within a certain range. Further, a second object of the present invention is to roughly pulverize a plate-like molded product of a thermosetting resin, and then pulverize between rolls having irregularities with a phase difference of 1/2 pitch formed on the roll surface. Accordingly, it is an object of the present invention to provide a method and an apparatus for producing beads for grinding and peeling an irregular polyhedron having a sharp ridge line. Disclosure of the invention
上記目的を達成するため、 本発明による ビーズは次のよ うな構成を具えたこ と を特徴とする。  In order to achieve the above object, the beads according to the present invention are characterized by having the following configuration.
すなわち、 本発明は、 熱硬化性樹脂成形物の粒径 1 0 0 0〜約 5. 0 m範囲の 破砕物で、各粒子が実質的に鋭利な稜線で囲まれた不定形で微細な多面体と され、 かつ分級段階ごとの粒度がある範囲内にほぼ均質化されている研削 · 剥離用ビー ズである。 熱硬化性樹脂中には、 パルプ及びガラス繊維布砕片を充填し、 さ らに カーボン、 人造黒鉛又は金属繊維を配合している。 具体的には、 凝縮後の熱硬化 性樹脂素材中に、 バルブ 3 0〜 4 0 %、 ガラス繊維布細片 0 . 1〜 0 . 5 %を配 合し、 同樹脂の熟成乾燥後に静電気発生抑制と帯電抑制のため炭素粉または導電 率 0 . 2〜0 . 3の人造黒鉛と、 比重を 1 . 8以上に上昇させるために金属紛又 は金属繊維 0 . 1〜0 . 5 %を配合する。  That is, the present invention relates to a crushed product of a thermosetting resin molded product having a particle size of 1000 to about 5.0 m, wherein each particle is substantially irregular and fine polyhedron surrounded by sharp ridges. This is a grinding / peeling bead whose grain size at each classification stage is almost homogenized within a certain range. The thermosetting resin is filled with pulp and glass fiber crushed pieces, and further contains carbon, artificial graphite or metal fibers. Specifically, 30 to 40% of a valve and 0.1 to 0.5% of a glass fiber cloth piece are mixed in the thermosetting resin material after condensation, and static electricity is generated after the resin is aged and dried. Compounded with carbon powder or artificial graphite with electrical conductivity of 0.2 to 0.3 for suppression and electrification suppression, and 0.1 to 0.5% of metal powder or metal fiber to increase specific gravity to 1.8 or more I do.
2 Two
訂正された用紙 (規則 91) 上記ビーズを製造するため、 本発明では、 熱硬化性樹脂のプ レー 卜状成形物.を サイ コロ状又はペ レ ッ ト状に破砕 (荒割) したのち、 これを向かい合う ロール表 面の凹凸が 1 / 2 ピッチの位相ズレをもって配置された多段式の破砕ロールで粉 砕するこ とによ り 、 鋭利な稜線を持つ不定形な多面体微細物 (ビーズ) とする。 本発明では、 熱硬化性樹脂と してメ ラ ミ ン樹脂 (メ ラ ミ ンーフオルムアルデヒ ド樹脂) 、 ユ リ ア樹脂 (尿素ー フ オルムアルデヒ ド樹脂) 、 フ エ ノ ール樹脂、 不 飽和ポリエステル、 アク リル、 グアナミ ン、 エポキシまたはポリ ウレタンなど 単独、 又は硬度 · 比重 ■ 粘度の異なる熱硬化性樹脂の数種を混合するこ とができ る。 これらの資材は、 使用によっても無公害であるもの、 利用範囲の拡大を 目的 と して電気的絶縁抵抗の大きなもの、 対アルカ リ · 酸に強いもの、 比較的対熱温 度が高いもの、 燃焼のおそれ (引火性、 発火性) がないもの、 毒性 (スチ レン、 エステル等) がないもの、 更には、 リ サイ クル使用の最中、 ノ ズルからの噴射の 衝撃で比較的粉状になり にく い粘性のある もの、 などの観点から選択される。 好 ま しく は、 メ ラ ミ ン樹脂にユ リ ア樹脂及び/又はフエノール樹脂を配合した樹脂 ブレー 卜状成形物を粉砕する力 、 あるいはメ ラ ミ ン樹脂、 ユ リ ア樹脂、 フ エ ノ ー ル樹脂の異種プレー トをそれぞれ粗く破砕し混合したのち、 粉碎して不定形な多 面体繊細物とするも のである。 Corrected form (Rule 91) In order to produce the beads, the present invention uses a thermosetting resin plate-like molded product. The obtained product is crushed (roughly divided) into a die shape or a pellet shape, and then the irregularities on the roll surface facing the same are obtained. Is crushed by a multi-stage crushing roll arranged with a 1/2 pitch phase shift to form irregular polyhedral fines (beads) with sharp ridges. In the present invention, as the thermosetting resin, melamine resin (melamine-formaldehyde resin), urine resin (urea-formaldehyde resin), phenol resin, and unsaturated resin Polyester, acrylic, guanamine, epoxy or polyurethane alone, or with hardness and specific gravity ■ Several kinds of thermosetting resins with different viscosities can be mixed. These materials are non-polluting even when used, have high electrical insulation resistance for the purpose of expanding the range of use, are resistant to alkaline acids, are relatively high in heat resistance, Non-flammable (flammable, ignitable), non-toxic (styrene, ester, etc.), and relatively powdery due to the impact of nozzle injection during recycling. It is selected from the viewpoints of difficult-to-viscous substances. Preferably, a force for crushing a resin plate-like molded product obtained by mixing a urea resin and / or a phenol resin with a melamine resin, or a melamine resin, a urea resin, or a phenol resin The different types of resin plates are coarsely crushed and mixed, and then ground to form irregular polyhedral fines.
鋭利多角面を持つビーズの吹き付けによるハンマー作用によつて研削 · 剥離効 果を発揮するが、 1 種または異種同硬度のビーズによるハンマー作用では、 「対 象物素地を傷める」 、 「ビーズ自体のク ラ ッ シャーを惹起させる」 という 2つの 問題を生じる。 そこで、 本発明者は、 異種硬度のビーズを数種混合させたビーズ を用いて研削又は剥離の実験を繰り返し行ったと ころ、 よ り硬度の低いビ一ズ群 が緩衝材となって対象素地を傷めず (緩衝効果) 、 ビーズ自体のクラ ッシュを防 止を発揮でき、 リ サイ クル回数が更に増加するこ とを確認した。  Grinding and peeling effects are exhibited by the hammer action of spraying beads with sharp polygonal faces, but the hammer action of beads of one or different kinds of the same hardness can damage the target substrate and the beads themselves. Cause a crusher ". Therefore, the present inventor repeatedly performed grinding or peeling experiments using beads in which several kinds of beads of different hardnesses were mixed, and found that a group of beads having a lower hardness served as a cushioning material and the target substrate was formed. It was confirmed that the beads were not damaged (buffering effect), could prevent the beads from crushing, and the number of recycles was further increased.
ビーズを製造する装置と しては、熱硬化性樹脂のプレー ト状成形物を約 2〜 4 m m角 (最大厚み 5 mm、 1 辺約 7 ,の扁平物) の不定形物なサイ コ ロ状ないしペ レ ツ ト状に破砕する ク ラ ッシャー部と、 ク ラ ッシャ一部で破砕された破砕物中の金 属 · 異物類除去する選別部と、 一対のロール表面に 1 Z 2 ピッチの位相ズレをも つ凹凸が形成されて選別部で選別された破砕物を粗砕する破砕ロールを具えた粗 砕部と、 粗砕部の破砕ロールと同様ロール表面に 1 Z 2 ピッチの位相ズレをも.つ 凹凸が形成されて粗砕部で得た粗砕物を粒径 1 0 0 0 〜 5 0 μ πιで鋭利な稜線を もつ不定形な微細多面体のビーズに加工する多段式粉砕ロール対を具えた粉砕部 と、 前記粉砕部の下流に配置した分級装置と、 から構成される。 As an apparatus for manufacturing beads, a plate-shaped molded product of thermosetting resin is an irregular shape of approximately 2 to 4 mm square (maximum thickness 5 mm, flat object with approximately 7 sides). A crusher section that crushes into a shape like a pellet, a sorting section that removes metal and foreign matter in crushed material crushed by a part of the crusher, and a 1Z2 pitch Coarse with crushing rolls for crushing the crushed material selected at the sorting unit with irregularities formed with a phase shift Similar to the crushing part of the crushing part and the crushing part, there is also a phase shift of 1 Z 2 pitch on the roll surface.The crushed material obtained in the crushing part with irregularities formed has a particle size of 100 to 500 μm. It comprises: a crushing section having a multi-stage crushing roll pair for processing into amorphous fine polyhedral beads having a sharp ridge at πι; and a classification device arranged downstream of the crushing section.
上記多段式粉砕ロール対を具えた破砕部は、 粉砕ロールの凹凸ピッチ及び対向 ロール間のク リ アラ ンスを最適なものに設定するこ とでビーズ粒径の変更、 調整 を行う粒度調整機構を具えている。  The crushing unit equipped with the above-mentioned multi-stage crushing roll pair has a particle size adjustment mechanism that changes and adjusts the bead particle size by setting the unevenness pitch of the crushing rolls and the clearness between the opposing rolls to be optimal. I have it.
更に、 このビーズ製造装置は、 粉砕部の下流に風力分級機、 電力分級機、 振動 篩い機等の分級装置を配置してビーズを分級し、 分級されたビーズを計量、 袋詰 して、 所定量の剥離用ビーズ包装品とする。 また、 分級各段階におけるメ ッシュ 上または下の細粒物を選別部の上流又は粗砕部の上流にリ ターンさせる循環ライ ンを備え、 ク ラ ッシャー部から分級装置までの各段階で生じる微細粒を含む粉塵 を粉塵処理装置に導く粉体輸送コ ンべャ又はダク トを備えている。  Furthermore, this bead manufacturing apparatus arranges a classifier such as an air classifier, an electric power classifier, and a vibrating sieving machine downstream of the pulverizing section to classify the beads, weigh and classify the classified beads. A fixed amount of bead packaging for peeling. In addition, a circulation line is provided to return the fines above or below the mesh in each classifying step upstream of the sorting section or upstream of the crushing section, and the fine particles generated in each step from the crusher section to the classifying apparatus are provided. Equipped with a powder transport conveyor or duct that guides dust containing particles to the dust treatment equipment.
前記分級装置と しては、 順次編み目 を細かく した数段の篩い網を有し、 各篩い 網上にあたる篩い機からシュー トを導出した振動篩い機が好適である。 第 1 段メ ッ シュアップのものは前記粉砕機に送られて再度粉砕され、 最下段メ ッシュアン ダ一は粉塵と して廃棄され、 第 2段以下の中間段メ ッシュ上のものはフ レコ ン詰 め機又は 2 0キロ袋詰め機に送られて計量、 袋詰めされて順次搬出され i。  As the classifying device, a vibrating sieve having several stages of sieves with successively finer stitches and deriving shoots from sieves on each sieve is suitable. The first-stage mesh-up is sent to the crusher and crushed again, and the lower-most mesh under is discarded as dust. Sent to a packing machine or 20kg bagging machine, weighed, packed in a bag, and sequentially carried out i.
この発明によって得られたビーズは、 各種金属 · 合成樹脂 · 木材 ' ガラスなど の製品を傷つけるこ となく研削し、 或いは塗装膜 ·接着剤層 ' シール . ワ ック ス ' コンク リー ト壁面又はタイルの汚れ、 落書き消しなどの瞬間剥離に用いる。 加工 対象品 (ワーク) と しては、 上記製品素材のほか、 装置 · 部品の塗装剥離、 サビ 落と し、 塗装不良品の再生、 電装品 · 成型品 · 金型 · ジグ等の洗浄、 研掃、 研磨、 路面標識 (白線等) や建造物の付着物又はシール等の剥離に使用される。 上記ビ ーズ使用による効果と しては、 研削 · 剥離ス ピー ドの迅速化によ り 、 作業時間の 短縮が可能になったこ と、 ワーク を傷つけないこ と、 コス トの削減、 粉塵や騒音 の発生が少ないこ と等が挙げられる。  The beads obtained by the present invention can be ground without damaging various metals, synthetic resins, wood, glass and other products, or painted films, adhesive layers, seals, waxes, concrete walls or tiles. Used for instantaneous peeling of stains and graffiti. In addition to the above-mentioned product materials, the products to be processed (workpieces) include coating and peeling of equipment and parts, rust removal, reproduction of defective coating, electrical components, molded products, molds, cleaning of jigs, etc. It is used for polishing, polishing, road marking (white line, etc.), and peeling off of adhering materials or seals on buildings. The advantages of using the above bead are that the speed of grinding and peeling has been shortened, making it possible to shorten the working time, not to damage the work, to reduce costs, and to reduce dust and dust. Low noise generation.
また、 本発明のビーズは、 下記のよ う に、 帯電防止性、 経済性及び研削 /剥離 性に優れ、 かつリサイ クル性に適している。 1 . まず、 本発明では、 この一般汎用品素原料 (厚み 2〜 5 m mのプレー 卜状.樹 脂成形品) の製造過程において、 特定の充填材を配合するこ と によ り剥離用ビー ズの剥離効果の向上をねら う。 Further, the beads of the present invention are excellent in antistatic properties, economical efficiency and grinding / peeling properties, and are suitable for recyclability, as described below. 1. First, in the present invention, in the production process of this general-purpose raw material material (plate-like resin molded product having a thickness of 2 to 5 mm), a specific filler is blended to form a peeling bead. The aim is to improve the effect of removing particles.
a . 充填材と して、 炭素粉 (カーボンブラック) を配合する (微量%) 。  a. Carbon powder (carbon black) is blended as filler (trace%).
目的:導電性の高い材料を配合するこ とでブラス ト時の静電気発生を抑制する。 b . 金属粉、 金属繊維を混入する (微量%) 。  Purpose: To suppress the generation of static electricity during blasting by blending highly conductive materials. b. Mix metal powder and metal fiber (trace amount).
目的 : 通常汎用品の比重が 1. 30〜 1. 48であるのに対し、 比重を 1.8〜2.0に上げ る。 ブラス ト対象物の素材表面を損傷させる懸念のない鉄製品研磨、 路面付着 物除去作業などに有効である。  Purpose: To increase the specific gravity to 1.8 to 2.0, while the specific gravity of general-purpose products is 1.30 to 1.48. This is effective for polishing iron products and removing road debris without worrying about damaging the material surface of the blast target.
c . パルプ ' セルロース繊維又はガラス繊維布細片を混合する。  c. Pulp 'Mix cellulose fiber or glass fiber cloth pieces.
目的 : 硬度、 機械的強度を増加させる。  Purpose: To increase hardness and mechanical strength.
2. メ ラ ミ ン樹脂とユ リ ア樹脂の混合でブラス 卜の衝撃強度を調整する。  2. Adjust the impact strength of the blast by mixing the melamine resin and the urine resin.
樹脂プレー 卜の成形:上記素原料を金型に充填し、加圧 (150〜200kg/ c m 2 ) 、 加熱 (130〜 165°C ) のも とで成形 (60〜 180秒 Zmra) する。 成形品の厚みによつ て成形時間は異なるが、 低温で成形時間を長くするこ とで、 高い硬度のものが 得られる。 Molding of resin plate: The above-mentioned raw material is filled in a mold, and molded (Zmra for 60 to 180 seconds) under pressure (150 to 200 kg / cm 2 ) and heating (130 to 165 ° C). The molding time varies depending on the thickness of the molded product, but a high hardness can be obtained by increasing the molding time at a low temperature.
3. 用途別に研削 · 剥離用ビーズの分級規格 〔出願人命名の M G (MA G I C- G EM) シリーズ番号〕 を示すと次のとおりである。  3. Classification standards for grinding and peeling beads for each application [MG (MA GIC-G EM) series number named by the applicant] are as follows.
a.—般金属用 (硬い素材) a.—For general metal (hard material)
M G— 0 1 5 0 0 μ mア ップ  MG — 0 150 0 μm Up
M G - 1 2 0 メ ッシュアンダー又は 8 4 0 μ mアップ  MG-12 0 Mesh under or 8 4 0 μm up
MG— 3 2 0〜 3 0 メ ッシュ ( 8 4 0〜 5 0 0 μ ιη)  MG—32 0 to 30 mesh (840 to 500 μιη)
b.アルミ (軟らかい素材) b. Aluminum (soft material)
G - 5 3 0〜 5 0 メ ッシュ ( 5 0 0〜 3 0 0 μ m)  G-530-500 mesh (500-300 μm)
MG— 7 5 0〜 7 0 メ ッシュ ( 3 0 0〜 2 1 2 μ m )  MG—750-70 mesh (300-212 μm)
c樹脂製品、 電子部品または塑造品などの高級品 c High-end products such as resin products, electronic components or molded products
M G - 1 0 7 0〜 ; 1 4 0 メ ッ シュ ( 2 1 2 0 6 m)  MG-107--; 140 mesh (2 120 m)
M G— 1 4 1 0 6 μ m以下。  MG — 14 16 μm or less.
4. リサイ クル性 ブラス ト作業時の対象物への吹き付けによ り、 ビーズが破砕されて粒径が小さ く なり、 かつ鋭利な稜線部分が丸みを帯びるが、 これを所定の粒度毎に篩い分 けて再利用する。 ビーズ径が細かく なつても個々の粒子の多面体形状、 研削 - 剥離効率は変わらない。 対象品の硬軟の程度、 ビーズの硬度、 比重、 空気圧力、 吹付け角度、 吹付け距離などによ り数回〜数十回再利用可能である。 図面の簡単な説明 4. Recyclability During the blasting operation, the beads are crushed and the particle size is reduced by spraying on the target object, and the sharp ridges are rounded. I do. Even if the bead diameter becomes smaller, the polyhedral shape of each particle and the grinding-peeling efficiency do not change. It can be reused several to several tens of times depending on the hardness of the target product, the hardness of the beads, specific gravity, air pressure, spray angle, spray distance, and other factors. BRIEF DESCRIPTION OF THE FIGURES
図 1 は、 本発明剥離用ビーズ製造方法のフローチャー トである。  FIG. 1 is a flowchart of the method for producing a peeling bead of the present invention.
図 2は、 本発明を実施するビーズ製造装置の概略を示す配置図である。  FIG. 2 is a layout diagram showing an outline of a bead manufacturing apparatus for carrying out the present invention.
図 3は、 図 2の粉砕部の斜視図である。  FIG. 3 is a perspective view of the crushing unit of FIG.
図 4は、 図 3 における粉砕ロール対の拡大斜視図である。  FIG. 4 is an enlarged perspective view of the grinding roll pair in FIG.
図 5は、 粉砕ロールの凹凸歯の拡大断面図である。  FIG. 5 is an enlarged cross-sectional view of the uneven teeth of the crushing roll.
図 6 は、 粉砕ロールの凹凸歯の変形を示す拡大断面図である。  FIG. 6 is an enlarged sectional view showing the deformation of the uneven teeth of the crushing roll.
図 7 は、 図 2における粉砕から包装まで各部の詳細を示す配置図である。  FIG. 7 is a layout diagram showing details of each part from pulverization to packaging in FIG.
図 8 は、 剥離用ビーズの一群を例示する拡大平面図である。 発明を実施するための最良の形態  FIG. 8 is an enlarged plan view illustrating a group of peeling beads. BEST MODE FOR CARRYING OUT THE INVENTION
図 1 はビーズの製造フ ロ ーを示す。  Figure 1 shows the bead production flow.
メ ラ ミ ンパゥダー 1 a、ホルマ リ ン 1 b及びアル力 リ又は酸触媒 1 cを反応槽 2 に 投入し重合凝縮させたのち、 混合槽 3 に移して充填材と して 3 0〜 4 0 %のパル ブ 3 aと、 0 . 1 〜 0 . 5 %のガラス繊維布細片 3 b を混練する。 熟成槽 4、 乾燥 機 5 を経た後、 ボールミ ル 6 内で、 ブラ ス 卜時の静電気発生を抑制するための炭 素粉 (導電率◦ . 3 %のカーボンブラ ック) と比重上昇用の金属繊維等 6 aを 0 . 1 〜 0 . 5 %配合する と と もに、 必要によ り着色材を配合する。  Melamine powder 1a, formalin 1b, and alcohol or acid catalyst 1c are charged into reaction tank 2 and polymerized and condensed, and then transferred to mixing tank 3 to be used as a filler. % Kneading of the pulp 3a and 0.1 to 0.5% of the glass fiber cloth strip 3b. After passing through the aging tank 4 and the drier 5, in the ball mill 6, carbon powder (a carbon black having a conductivity of 0.3%) for suppressing static electricity generation during blasting and a carbon powder for increasing the specific gravity are used. 0.1 to 0.5% of metal fiber 6a is blended, and a coloring material is blended if necessary.
篩分け部 7で異物を除去して成形材料 (メ ラ ミ ン樹脂) 8 とする。 これとほぼ 同様な手順で得た成形材料 (ユ リ ア樹脂) 8 aを加え混練 8 c し、 加圧 ·加熱して 成形加工して硬度、 比重の異なる厚さ 2〜 5 mmの樹脂プレー 卜 1 0 を得る。  The foreign matter is removed at the sieving section 7 to obtain a molding material (melamine resin) 8. Add molding material (urea resin) 8a obtained by almost the same procedure as above, knead 8c, pressurize and heat and mold to form a resin with a thickness of 2 to 5 mm with different hardness and specific gravity Get 10
素原料をプレー ト状物に成形加工し、 破砕 (クラシヤー) から粉砕、 包装まで の工程を一貫して行う こ とに限らず、 幾つかの工程に分けるカ 各工程ごとに分  The raw material is formed into a plate-like material, and the process from crushing (crushing) to crushing and packaging is not only performed consistently, but it is divided into several processes.
6 6
た 紙 (規則 91 ) 業して最終製品ビーズを製造するこ とができる。 Made paper (Rule 91) To manufacture finished product beads.
次に、 上記各プレー 卜 1 0を約 2〜 4 mm角のサイ コロ状又はペレツ 卜状にそれ ぞれ破砕するクラ ッシャ 1 1 、 破砕物を混合するプレン ド部 1 2、 異物を磁気選 別する選別部 1 4、 粗砕加工 1 5、 数段の破砕ロールによる粉砕加工 1 6、 篩分 け 1 8 、 計量 2 3、 包装 2 4 を経て搬出 2 5 される。  Next, a crusher 11 for crushing each of the above-mentioned plates 10 into a die or a pellet of about 2 to 4 mm square, a pre-mixing section 12 for mixing crushed materials, and a magnetic separation for foreign substances. Separation section 14, crushing 15, crushing with several crushing rolls 16, sieving 18, weighing 23, packing 24, and then unloaded 25.
[ビーズ製造装置〕  [Bead production equipment]
図 2はビーズ製造装置の概略を示す正面図、 図 3は図 2における粉砕部の拡大 斜視図、 図 4は図 3における粉砕ロールの拡大断面図である。  FIG. 2 is a front view schematically showing a bead manufacturing apparatus, FIG. 3 is an enlarged perspective view of a crushing unit in FIG. 2, and FIG. 4 is an enlarged cross-sectional view of a crushing roll in FIG.
図 2 に示すよ う に、 硬度、 材質の異なる熱硬化性樹脂成形材料の複数種の樹脂 プレー ト 1 0 (厚み 3〜 5 mm、 3 0 0 X 5 0 0 mm) をク ラ ッシャー部 1 1 で約 2 〜 4 mm角 (最大厚み 5 mm X l 辺 7 mmの扁平物) の不定形物なサイ コロ状ないしぺ レッ ト状に破砕 (荒割) して混合部 1 2に投入する。 図 2では、 A、 B、 C、 D、 E、 Fの 6種の樹脂プレー 卜 1 0 を図示したが、 これらは同じ材質のものに限ら ず、 2種以上の材質のものを用いてもよい。 すなわち、 樹脂プレー ト 1 0は、 メ ラ ミ ン榭脂、 ユ リ ア樹脂、 フエ ノール樹脂、 不飽和ボリエステル、 ァク リ ノレ、 グ アナミ ン、 エポキシまたはポリ ウ レタン等の成形材料、 から選ばれたものを使用 するが、 メ ラ ミ ン 6 0〜 8 0 % ]^ュリ ア 4 0〜 2 0 %を混合したもの、 あるレ、は メ ラ ミ ン、 ユ リ ア、 フニノール樹脂を混合するなど、 2種以上の混合材料を成形 したものでもよレ、。 また、 メ ラ ミ ン樹脂プレー ト とユリ ア樹脂プレー 卜またはフ エ ノール樹脂プレー トをそれぞれク ラシヤーで破砕したのち混合してもよい。 ク ラ ッシャー 1 1 は、 従来のハンマーミ ル、 円盤粉砕機、 コーン粉砕機、 オシ ユ レータ等とは異なり 、 ロータに数枚の可動刃 (鋸歯状刃をもつク ローズドフラ ッ トカ ツタ) を取り付け、 ロータの回転によ り 固定刃との間で破砕するタイプ(図 示省略) が使用される。 ハンマー式ク ラ ッシャー等は、 粉砕品に多く のひび割れ が現れるのみか、 粉砕時の粉塵の発生が甚だしいため有効ではない。 なお、 樹脂 プレー ト 1 ◦は、 シー ト状物に限らず、 熱硬化性樹脂材料の破砕物、 例えば樹脂 材料の成形時に発生するスプル一、 ランナー及び成形不良品等を事前に破砕する こ とによ り、 所定品質の約 2 mm角の不定形物が素材と して安定に供給可能であれ ば、 図 2 中のク ラ ッシャー部 1 1 を省略して直接混合部 1 2に投入してもよい。 〔破砕物の粉碎 · 篩分け〕 As shown in Fig. 2, several types of resin plates 10 (thickness: 3 to 5 mm, 300 x 500 mm) of thermosetting resin molding materials with different hardness and material are applied to the crusher section 1. It is crushed (roughly divided) into an irregular die or pellet of approximately 2 to 4 mm square (maximum thickness 5 mm X l side 7 mm flat) with 1 and put into the mixing section 12 . In FIG. 2, six types of resin plates 10 of A, B, C, D, E, and F are illustrated, but these are not limited to the same material, and two or more types of materials may be used. Good. That is, the resin plate 10 is selected from molding materials such as melamine resin, urea resin, phenol resin, unsaturated polyester, acrylate, guanamine, epoxy or polyurethane. 60% to 80% of melamine mixed with 40% to 20% of urea, one resin is made of melamine, urea, and funinol resin. It may be a mixture of two or more types of mixed materials, such as mixing. The melamine resin plate and the urea resin plate or the phenol resin plate may be crushed by a crusher, and then mixed. Unlike conventional hammer mills, disk crushers, cone crushers, oscillators, etc., the crusher 11 has several movable blades (closed flat cutters with serrated blades) attached to the rotor. A type that crushes between the fixed blade and the fixed blade by rotation of the rotor (not shown) is used. Hammer type crushers are not effective because only a lot of cracks appear in the crushed product or dust is generated during crushing. The resin plate 1 ◦ is not limited to sheet-like material, but should be used in advance to crush crushed thermosetting resin materials, such as sprues, runners and defective moldings generated during molding of resin materials. As a result, if it is possible to stably supply an irregular shaped material of approximately 2 mm square of a predetermined quality as a material, the crusher unit 11 in Fig. 2 is omitted and the mixture is directly introduced into the mixing unit 12. You may. [Crushing and sieving of crushed material]
混合部 1 2 の下部に自動供給機 1 3 と整流フィーダ 1 3 a と を設ける。 整流フ ィーダ 1 3 a によって流下する破砕物を、 ほぼ均一厚さの層状に整流させて金 厲 ' 異物類除去用の選別部 1 4に送る。 選別部 1 4の下方には粗砕部 (一対の破 砕ロール、 静電気除去装置付き) 1 5、 粉砕部 (多段式破碎ロ ール対、 静電気除 去装置付き) 1 6 を設け、 更に切替弁 1 7を介して篩分け部 1 8 に連ねる。 篩分部 1 8は、 微細粒を分級する風力分級機 2 1 と、 微細粒よ り大径粒を分級 する電力分級機 2 2 とで構成される。 分級された粒体 (剥離用 ビーズ) は、 包装 出荷部にあたる自動計量機付き袋詰 2 3、 自動袋口縫機 2 3 によ り、 所定容量 の剥離用ビーズ包装品となって搬送機 2 5等を用いて場外に搬出される。  An automatic feeder 13 and a rectifying feeder 13a are provided below the mixing section 12. The crushed material flowing down by the rectifying feeder 13a is rectified into a layer having a substantially uniform thickness, and sent to the metal 厲 'sorter 14 for removing foreign matter. Below the sorting unit 14, a crushing unit (with a pair of crushing rolls and a static eliminator) 15 and a crushing unit (multi-stage crushing roller pair and a static eliminator) 16 are provided, and further switched It is connected to a screening section 18 through a valve 17. The sieving section 18 is composed of an air classifier 21 for classifying fine particles and a power classifier 22 for classifying large-diameter particles from fine particles. The classified granules (beads for peeling) are packaged into peeling beads of a predetermined volume by the bagging machine 23 with an automatic weighing machine, which corresponds to the packaging shipping department, and the automatic bag mouth sewing machine 23, and the transporter 2 It is carried out of the site using 5 mag.
電力分級機 2 2 のメ ッ シュ上の細粒物を循環パイプ 2 6 a に導入して選別部 1 4 の上流にあるホッパ付き整流フ ィーダ 1 3 a にリ ターンさせ、 また、 風力分級 機 2 1 のメ ッシュ上の細粒物を循環パイプ 2 6 bに導入して粗砕部 1 5の上流に リ ターンさせる。 各段階で生じる粉塵は、 図 2の点線に示すよ う なダク ト 2 7 を 通じて上方の粉塵処理装置 (分離装置) 2 8に送り、 所定の粒度以上のものを混 合機 1 2に戻す、 一方所定の粒度以下の微粉を集塵装置 2 9 に送って処分する。  The fines on the mesh of the electric power classifier 22 are introduced into the circulation pipe 26a and returned to the rectifier feeder 13a with hopper upstream of the sorting section 14a. The fine particles on the mesh of 21 are introduced into the circulation pipe 26 b and returned upstream of the crushing section 15. The dust generated at each stage is sent to an upper dust treatment device (separation device) 28 through a duct 27 as shown by the dotted line in Fig. 2, and the dust having a predetermined particle size is passed to the mixer 12. On the other hand, the fine powder having a predetermined particle size or less is sent to the dust collector 29 for disposal.
〔粗砕ロールの構成〕  [Configuration of crushing roll]
図 2 において、 1 5 a 、 1 5 a は粗砕ロール、 1 5 bはホ ッノ 、 1 5 c はホッ バから流下する粗砕物をほぼ均一厚さの層状に整流させる整流フィーダである。 粗砕ロール 1 5 a は、 粉砕ロールについて後記するよ う に、 ロール表面の円周上 定間隔に母線方向に延びる教条の横溝 3 5 を有し、 かつロール表面に多数の凹凸 3 6 を形成させている。  In FIG. 2, 15a and 15a are crushing rolls, 15b is a honno, and 15c is a rectifying feeder for rectifying the crushed material flowing down from the hobber into a layer having a substantially uniform thickness. The crushing roll 15a has lateral grooves 35 extending in the generatrix direction at regular intervals on the circumference of the roll surface, as described later for the crushing roll, and has many irregularities 36 on the roll surface. Let me.
ク ラ ッ シャー部 1 1 で 2 〜 4 mm角のサイ コロ状ないしペ レ ツ ト状にされた破砕 物を、 粗砕ロール 1 5 a、 1 5 aの回転によってほぼ 2 m m角に粗砕する。  The crushed pieces of 2 to 4 mm square die or pellets at the crusher section 11 are crushed into approximately 2 mm square by rotating the crushing rolls 15a and 15a. I do.
〔粉砕部の構成〕  [Configuration of crushing unit]
図 3 は、 ビーズ製造装置における粉砕部 1 6 の拡大斜視図、 図 4は架砕ロール 対の斜視図である。 フ レーム 3 0に、 一対の粉砕ロ ール 3 1 、 3 1 、 3 2 、 3 2 、 3 3 、 3 3を上下 3段に横架する。 各ロール表面は円周上定間隔に母線方向に延 びる数条 ( 4個) の横溝 3 5 と、 ロール表面に多数の山形状凹凸 3 6 を有してい る (図 5 ) 。 後述のよ う に、 イ ンデッ ク スゲージダイヤル 3 7 を操作して口一.ル 間隙を 0 . 1 ないし 0. 2 mmに調整する (図 4 ) 。 図 6はロール表面に多数の角 形状凹凸 3 6 a を形成させたものを示す。 FIG. 3 is an enlarged perspective view of the crushing section 16 in the bead manufacturing apparatus, and FIG. 4 is a perspective view of a crushing roll pair. A pair of pulverizing rolls 31, 31, 32, 32, 33, and 33 are laid on the frame 30 in three vertical stages. Each roll surface has several (four) lateral grooves 35 extending in the generatrix direction at regular intervals on the circumference, and a number of mountain-shaped irregularities 36 on the roll surface. (Fig. 5). Ni will Yo described later, the mouth one by operating the Lee Nde' click scan gauge dial 3 7. Le gap 0.1 to adjust to 0. 2 m m (Figure 4). Figure 6 shows a roll with a number of angular irregularities 36a formed on the roll surface.
各ロ ールにス ク レーパ 3 8 を接近配置する。  A scraper 38 is placed close to each roll.
なお、 図 3 中、 4 0は減速機付きモータ、 4 1 、 4 2、 4 3は各段の口ール軸、 4 4はモータ と第 1 段ロール軸のスプロケッ 卜間に掛けたチェーン、 4 5は向か い合う各段ロール軸のスプロケッ ト間に掛けたチヱーンである。 向かい合う第 1 段ロール軸間には、 同期回転用歯車 (図示省略) を嚙み合わせている。  In Fig. 3, 40 is a motor with a speed reducer, 41, 42, and 43 are portal shafts of each stage, and 44 is a chain hung between the motor and the first stage roll shaft sprocket. 45 is a chain hung between the sprockets of the roll rollers facing each other. A synchronous rotation gear (not shown) is interposed between the opposing first-stage roll shafts.
〔粉砕ロールのサイズ〕  [Size of grinding roll]
粉砕 (加工) 部 1 6では、 第 1 段から第 3段に向かってロールの凹凸ピッチを 漸減させる一方ロール回転数を漸増させる。例えば、各ロールの径は 1 5 0 mraで、 各段の凹凸ピッチ及び回転数を示すと下記のとおりである。  In the crushing (processing) unit 16, the roll pitch is gradually increased while the roll pitch is gradually reduced from the first stage to the third stage. For example, the diameter of each roll is 150 mra, and the uneven pitch and rotation speed of each stage are as follows.
第 1段 : ピッチ 2.0mm, V 1 = 5 0 0〜 5 2 0 rpm ( 5 1 7 rpm) 。 First stage: pitch 2.0 mm, V 1 = 500 to 52 rpm (5 17 rpm).
第 2段 : ピッチ 1.2mm、 V 2 = V i X 1 . 2〜 1 . 3 ( 6 3 2 rpm) 。 Second stage: pitch 1.2 mm, V 2 = V i X 1.2 to 1.3 (632 rpm).
第 3段 : ピッチ 0.6mm, V 3 = V i X 1 . 5前後 ( 7 7 2 rpm) 。 Third stage: pitch 0.6 mm, V 3 = around V i X 1.5 (772 rpm).
なお、 粗砕部 1 5のロールも同様の凹凸が形成されている。  The rolls of the crushing section 15 also have the same irregularities.
製造工程では粗砕部、 粉砕部で数段階の破砕ロールによ り均質化をはかる。 ビ ーズ形状の大き さの均質化をはかるためロール形状 (凹凸ピッチ) 及びロール間 ク リ アラ ンスを重要視し、 その結果ビーズ粒径 (サイズ) の変更が容易になった。 運転する前に、 各段ロールの相対する山と谷 3 6、 3 6 とが向かい合う位置に 正しく設定 (目合わせ) しておく必要がある。 こ のため、 軸方向可動に取り付け た一方のロール (例えば図 2の各段後側のロール) の軸受部に、 ロールの軸心方 向に延びるアジャス トボル 卜 (図示省略) を設け、 このアジャス トポル トの先端 をフ レームの側壁側に突き当てて目合わせ調節機構を構成させている。 マ二ユア ル操作でア ジャ ス ト ポル ト の突き当て有効長さを加減して、 後側ロールを軸心方 向に僅かに移動させるこ とでロール凹凸(山と谷)の目合わせ操作が達成される。 また、 ロール間のク リ アラ ンスは、 榭脂の硬度、 材質、 粒度等によって調整す るが、 通常 0. 1 1 〜 0 . 3瞧程度又はそれ以上である。 前後方向可動に支持さ れた他方のロール (例えば図 2の各段前側のロ ール 3 1 ) の左右両軸受部に調節 用ネジ 3 7 aを固着し、 その先端にそれぞれイ ンデックスハン ドル (インデックス ゲージダイアル) 3 7、 3 7 を設けている。 ク リ アランスを調整するには、 イ ン デッ ク スハン ドルを回動して左右又は左右何れかの軸受部を前後方向に移動する こ とで行われる。 なお図 3では、 フレーム右側のインデックスハン ドル 3 7 、 3 7のみを示し、 左側のインデックスハン ドルの図示を省略している。 In the manufacturing process, homogenization is performed using several stages of crushing rolls in the crushing and crushing sections. In order to homogenize the bead shape, the roll shape (concavo-convex pitch) and the clearance between rolls were emphasized, and as a result, the bead particle size (size) was easily changed. Before operation, it is necessary to correctly set (match) the positions where the peaks and valleys 36, 36 facing each other of the rolls face each other. For this reason, an adjustment bolt (not shown) is provided on the bearing portion of one of the rolls (for example, the roll on the rear side of each stage in FIG. 2) which is mounted so as to be movable in the axial direction and extends in the axial direction of the roll. The end of the top is abutted against the side wall of the frame to form the alignment mechanism. Adjusting the effective length of the adjust port by manual operation, and slightly moving the rear roll in the axial direction, aligning the roll unevenness (peaks and valleys). Is achieved. The clearance between the rolls is adjusted according to the hardness, material, grain size, etc. of the resin, but is usually about 0.11 to 0.3 mm or more. Adjusted to the left and right bearings of the other roll (for example, the roll 31 in front of each stage in Fig. 2) supported to be movable in the front-rear direction Screw 37a is fixedly attached, and index handles (index gauge dials) 37, 37 are provided at the ends thereof. Adjustment of the clearance is performed by rotating the index handle and moving the left or right or left or right bearing in the front-rear direction. In FIG. 3, only the index handles 37 and 37 on the right side of the frame are shown, and the index handle on the left side is not shown.
〔製造工程〕  〔Manufacturing process〕
製造工程では粗砕部、 粉砕部で数段階の特殊ロールによ り均質化をはかる。 ビ —ズ形状の大き さの均質化をはかるためロール形状 (ピッチ、 ク リ アランス) を 重要視し、 その結果ビーズ粒径 (サイズ) の変更が容易になった。 従来のハンマ —ミ ル、 円盤粉砕機、 コーン粉砕機、 オシユ レータ等とは異なる粉砕方法を採用 した。 また、 粗砕加工部、 粉砕加工部では、 材料へ圧力、 衝撃、 剪断、 摩擦の生 じる場所 (部位) での静電気発生を防止する静電気除去装置を設ける。  In the manufacturing process, the homogenization is performed using special rolls of several stages in the crushing and crushing sections. The roll shape (pitch, clearance) was emphasized in order to homogenize the bead size, and as a result, the bead particle size (size) was easily changed. It uses a different grinding method than conventional hammer mills, disk grinders, cone grinders, oscillators, and so on. In the crushing section and crushing section, a static electricity eliminator is installed to prevent static electricity from being generated in places (sites) where pressure, impact, shear, and friction occur on the material.
〔粒体分離〕  (Particle separation)
ク ラ ッシャー部から分級機 (篩分け部) までの各段階で生じる微細粒を含む粉 塵を、 例えば、 特許第 2 8 9 1 6 3 1 号 (特開平 8 — 2 5 2 2 3号) に開示した よ う な粒体分離装置 (粉塵処理装置) で再利用可能な粒体ビーズと粉塵とに分離 する。  Dust containing fine particles generated at each stage from the crusher section to the classifier (sieving section) can be extracted from, for example, Patent No. 2891 163 1 (Japanese Patent Application Laid-Open No. Hei 8-252223). The particles are separated into reusable granular beads and dust by a granular separation device (dust treatment device) as disclosed in (1).
すなわち、 この粒体分離装置は、 円筒状の分離容器 (分離室) と ; 前記分離容 器の外周に形成された格納容器と ; 破砕工程中に生じるダス ト及び再生可能な微 細な粒体 (ビーズ) を、 圧縮空気と と もに前記分離容器內に吹き込むため、 格納 容器の側壁を貫いて分離容器に取付けた搬入管と ;前記分離容器内に配置されて、 前記搬入管から送入されたダス ト及び再生可能なビーズを質量の差によって拡散 分離する拡散部材であって、 間隔をあけて上下数段に重ねたパンチング孔又はス リ ッ 卜付き円板群からなる拡散部材と ;前記格納容器の頂部近く の側壁に設けた、 ダス 卜の排出管と ; 塵埃分離後の再生可能なビーズを収容すべく 、 前記格納容器 と分離容器との下部にまたがって配設されたタンク と、 から構成されている。  That is, the granular material separation device includes: a cylindrical separation container (separation chamber); a storage container formed on the outer periphery of the separation container; dust and renewable fine particles generated during the crushing step. (Beads) are blown into the separation container (2) together with compressed air, so that a carry-in tube is attached to the separation container through the side wall of the storage container; and is arranged in the separation container and is delivered from the carry-in tube. A diffusion member for diffusing and separating the dust and renewable beads obtained by the difference in mass, comprising a group of discs with punching holes or slits which are spaced apart from each other and stacked in several stages; A discharge pipe for dust provided on a side wall near the top of the containment vessel; and a tank disposed below the containment vessel and the separation vessel to accommodate renewable beads after dust separation. Is composed of I have.
〔分離容器の構成〕  (Configuration of separation vessel)
また、 分離容器 (分離室) は、 前記拡散部材を通過しなかった塵埃を格納容器 の頂部近く の排出管側に排出すベく 、 前記拡散部材のビーズ受入れ面よ り も上方 に第 1排出口を備え、 前記格納容器が、 拡散部材のパンチング孔又はス リ ツ 卜を 通過して再利用可能ビーズ収納タンク内に流下し浮遊する塵埃を排出管側に排出 すべく 、 当該収納タ ンクの上板に当たる格納容器の底部に開口する第 2排出口を 備えている。 In addition, the separation container (separation chamber) discharges dust that has not passed through the diffusion member to a discharge pipe near the top of the storage container, and is higher than a bead receiving surface of the diffusion member. The storage container is further provided with a first discharge port, and the storage container is configured to discharge dust floating through the punching holes or slits of the diffusion member into the reusable bead storage tank and floating to the discharge pipe side. A second outlet is provided at the bottom of the containment tank, which is the upper plate of the storage tank.
上記分離装置によれば、 分離容器内に配置した上下数段のパンチング孔または ス リ ッ ト付き円板群からなる拡散部材によ り、 再利用可能ビーズと塵埃が、 極め て効率的に拡散されるので、 分離精度を高き維持するこ とができる。  According to the above separation device, the reusable beads and dust are extremely efficiently diffused by the diffusion member composed of a plurality of upper and lower punching holes or a group of disks with slits arranged in the separation container. As a result, the separation accuracy can be maintained at a high level.
上記粒体分離装置 (粉塵処理装置) 2 8 の詳細は、 前記特許第 2891631号に開示 されているので図示を省略したが、 各段階に発生する再利用可能なビーズと粉塵 の混合物は、 吸引ダク ト 2 7 によって分離容器 (分離室) 内へ搬送される。 集塵 機 2 9 を稼動させているため、 分離容器内は負圧状態となっている。 従って、 吹 込口から吹き込まれたビーズおよび粉塵の混在物は、 高速で分離容器の内壁、 内 蓋下面、 最上部の拡散板の上面に、 激しく衝突し拡散する。 この時、 粉塵は、 第 1排出口 4 6から吹出され、 分離容器の外上面と格納容器の外蓋裏面との間の空 間を通って排出口 4 6 に至り集塵機 2 9 に吸引される (図 2 ) 。  The details of the particle separation device (dust treatment device) 28 are omitted from the drawings because they are disclosed in the aforementioned Japanese Patent No. 2891631, but the mixture of reusable beads and dust generated at each stage is suctioned. It is transported into the separation vessel (separation chamber) by duct 27. Since the dust collector 29 is operating, the inside of the separation vessel is under negative pressure. Therefore, the mixture of beads and dust blown from the inlet violently collides with the inner wall of the separation container, the lower surface of the inner lid, and the upper surface of the uppermost diffusion plate and diffuses at high speed. At this time, the dust is blown out from the first discharge port 46, passes through the space between the outer top surface of the separation container and the back surface of the containment container, reaches the discharge port 46, and is sucked into the dust collector 29. (Figure 2 ) .
〔拡散板の構成 · 作用〕  [Structure and operation of diffusion plate]
次に、 質量の大きい再利用可能粒体と、 第 1排出口 4 6から排出されなかった 粉塵は、 拡散板 (図示省略) の各パンチ孔又はス リ ッ トを通り 、 拡散板上へと落 下し拡散板上面と衝突し拡散する。 こ こで、 再度、 質量の小さい粉塵は舞上げら れ、 拡散板の各パンチ孔又はス リ ッ 卜を通り、 第 1 排出口 4 6から排出される。 このよ う な工程を経て、 最後に、 拡散板を通過した、 再利用可能粒体と残り の 小量の塵埃は、 ホッパタンクの下方へと落下するが、 その際、 質量の小さい塵埃 は、 第 2排出口 4 7から吹出され、 分離容器 2 8の外壁と内壁の間の空間を通つ て粉塵排出口から排出される。  Next, the reusable particles having a large mass and the dust not discharged from the first discharge port 46 pass through the respective punch holes or slits of the diffusion plate (not shown) and pass onto the diffusion plate. It falls and collides with the upper surface of the diffuser plate to diffuse. Here, the low-mass dust is again blown up, and is discharged from the first discharge port 46 through each punch hole or slit of the diffusion plate. Through these steps, finally, the reusable particles and the remaining small amount of dust that have passed through the diffusion plate fall down to the lower part of the hopper tank. (2) It is blown out from the discharge port (47) and discharged from the dust discharge port through the space between the outer wall and the inner wall of the separation container (28).
[ビーズの再利用〕  [Reuse of beads]
ブラス 卜作業時のビーズ再利用について述べる。 対象物への吹き付けによ り 、 ビーズが破砕されて粒径が小さ く なり 、 かつ鋭利な稜線部分が丸みを帯びるが、 これを前記分離装置を用いて篩い分けてビーズを繰り返し再利用する。 ビ一ズ径 が細かく なつても個々の粒子の多面体形状、 研削 · 剥離効率は変わらない。 対象 品の硬軟の程度、 ビーズの硬度、 比重、 空気圧力、 吹付け角度、 吹付け距離な.ど によ り数回〜数十回 (例えば 6 0回) 再利用可能である。 ただし、 M G— 1 4 ( 1 0 6 μ m以下、 例えば約 5 0 μ m ) は 1 回のみの使用でリサイ クルしない。 This section describes the reuse of beads during blasting. By spraying on the target object, the beads are crushed to reduce the particle size, and the sharp ridge portion is rounded. The beads are repeatedly reused by sieving using the separation device. Even if the bead diameter becomes smaller, the polyhedral shape of each particle and the grinding / peeling efficiency do not change. Target It can be reused several to several tens times (for example, 60 times) depending on the hardness of the product, the hardness of the beads, specific gravity, air pressure, spray angle, spray distance, etc. However, MG-14 (106 μm or less, for example, about 50 μm) does not recycle only once.
本実施例では、 第 1排出口 4 6だけではなく 、 拡散部材を通過した塵埃及び圧 送空気を排出する第 2排出口 4 7が設けられている (図 2 ) 。 従って、 塵埃を吹 出す機会が増大し、 再利用可能粒体への塵埃の混入を防止する。  In this embodiment, not only the first discharge port 46 but also a second discharge port 47 for discharging dust and compressed air passing through the diffusion member is provided (FIG. 2). Therefore, the chance of blowing dust increases, and dust is prevented from being mixed into the reusable granules.
第 1排出口 4 6力 S、 拡散部材の粒体受入れ面である拡散板の上面と対向して配 設されている。 従って、 拡散部材によ り拡散された塵埃を容易に吹出すことがで きる。 また、 第 1 排出口 4 6力 拡散部材の粒体受入れ面である拡散板の上面よ り も上方に配設されている。 従って、 質量の大きい再利用可能ビーズが第 1排出 口 4 6から吹出される可能性が低く なり、 結果と して、 分離精度を高める。  The first discharge port 46 is arranged to face the upper surface of the diffusion plate, which is the particle receiving surface of the diffusion member. Therefore, the dust diffused by the diffusion member can be easily blown out. In addition, the first discharge port 46 is disposed above the upper surface of the diffusion plate, which is the particle receiving surface of the diffusion member. Therefore, the possibility that the reusable beads having a large mass are blown out from the first outlet 46 is reduced, and as a result, the separation accuracy is improved.
また、 第 2排出口 4 7が、 再利用可能粒体収納タ ンクであるホツバの上方に設 けられている。 従って、 質量の大きい再利用可能粒体が第 2排出口 4 7から吹出 される可能性が低く なる。  In addition, a second discharge port 47 is provided above the hobba, which is a reusable granule storage tank. Accordingly, the possibility that the reusable granules having a large mass are blown out from the second discharge port 47 is reduced.
〔粉砕から包装まで各部の配置〕  [Disposition of each part from crushing to packaging]
図 7は、 粉砕から包装までの別例を示す各機器の配置図である。 図 2 、 3 に示 したロール式粉砕機 1 6 によって粉砕されたビーズは振動篩 2 0によって分級さ れる。 この振動篩機 2 0は内部に、 順次編み目を細かく した数段の篩い網 5 0〜 5 3 (例えば、 6 、 2 0 、 3 2、 5 0 メ ッシュ) を有し、 各篩い網上にあたる篩 い機外壁からシュー ト 5 0 a〜 5 3 aと最下段篩い下からシュー ト 5 4を導出して コンべャ又はダク 卜 5 5〜 5 9にそれぞれ接続する。 振動篩機 2 0 の内部に設け た各段篩い網 5 0〜 5 3は任意のメ ッシュのものに交換でき、 1 0メ ッシュ以下 から 1 5 0 メ ッシュの範囲内でビーズ大き さを分級するこ とが可能である。  FIG. 7 is an arrangement diagram of each device showing another example from crushing to packaging. The beads crushed by the roll crusher 16 shown in FIGS. 2 and 3 are classified by the vibrating sieve 20. This vibrating sieve 20 has several stages of sieve nets 50 to 53 (for example, 6, 20, 32, 50 meshes) in which the stitches are sequentially made fine, and hits each sieve net. The shoots 50a to 53a from the outer wall of the sieve and the shoots 54 from the bottom of the lowermost sieve are led out and connected to the conveyor or ducts 55 to 59, respectively. Each sieve mesh 50 to 53 provided inside the vibrating sieve 20 can be replaced with any mesh, and the bead size is classified within the range from 10 mesh or less to 150 mesh. It is possible to do so.
図 7 における粉砕機 1 6及び篩分け機 2 0は、 2系統又はそれ以上並設可能で あるが、 説明を簡単にするため、 1 系統にした場合を図示し説明する。  The crusher 16 and the sieving machine 20 in FIG. 7 can be installed in two or more lines, but for simplicity of explanation, the case where only one line is used is illustrated and described.
ダク 卜 5 5 に投入された 6 メ ッシュ以上のものは、 異物を除去したのち粗砕機 1 5、 粉砕機 1 6 に送られて再度粉砕され、 粉体輸送コ ンべャ又はダク ト 5 6 に 投入された 6 メ ッシュ以下〜 2 0 メ ッシュ上のものは篩分けによって M G— 7 , 1 0, 1 4 と される。 コンべャ 5 7 に投入された 2 0メ ッシュ以下〜 3 2 メ ッシ ュ上のものは MG— 3 と して第 1 の袋詰めライン 6 0に送られ、 コンペャ 5 8.に 投入された 3 2 メ ッシュ以下〜 5 0メ ッシュ上のものは MG— 5 と して第 2の袋 詰めライ ン 8 0に送られる。 Those with 6 mesh or more put in the duct 55 are sent to the crusher 15 and the crusher 16 where the foreign substances are removed and then crushed again.The powder transport conveyor or duct 56 Anything from 6 mesh to 20 mesh that has been put into the mash is classified as MG-7,10,14 by sieving. 20 mesh or less thrown into conveyor 57 ~ 32 mesh The items on the mesh are sent to the first bagging line 60 as MG-3, and those below the 32 mesh to 50 mesh that are input to the conveyor 58 are called MG-5. Sent to the second bagging line 80.
第 1 の袋詰めライ ン 6 0は、 コンべャ 5 7の下流端に設けた切替ダンバ 6 1 に よって ュ トン ' フ レコン (フ レキシブルコンテナ) 詰機 6 2 と 2 0 k g袋詰機 7 0に連接されている。 フ レコン詰機 6 2はレベル検知器付きホッパ 6 3、 投入ダ ンノ、° 6 4、 フ レコン袋 6 5、 台秤 6 6及び搬送コ ンべャ 6 7から構成され、 2 0 k g袋詰機 7 0はレベル検知器付きホッパ 7 1 、 計量並びに縫製ミ シン付きホッ ノ 7 2、 袋 7 4及びベル ト コンべャ 7 5、 7 6から構成されている。  The first bagging line 60 is provided by a switching damper 61 provided at the downstream end of the conveyor 57, and is provided with a double-toned flexible container (flexible container) filling machine 62 and a 20 kg bagging machine 62. Connected to 0. The frecon packing machine 62 consists of a hopper with a level detector 63, a loading dang, ° 64, a frecon bag 65, a platform scale 66 and a conveyor 67, and a 20 kg bag filling machine Reference numeral 70 denotes a hopper 71 with a level detector, a hopper 72 with a weighing and sewing machine, a bag 74 and belt conveyors 75, 76.
第 2の袋詰めライ ン 8 0は、 粉体輸送コ ンべャ 5 8の最下端に設けたレベル検 知器付きホ ッノ 8 1 、 スク リ ューコンべャ 8 2、 投入ダンバ 8 3及び計量器付き ホ ッ ノ、° 8 4によって構成されており、 2 0 k g包装袋 8 6がコ ンペャによ り順次 搬出される。  The second bag-filling line 80 is a hopper 81 with a level detector, a screw conveyor 82, an input dumper 83, and a hood 81 with a level detector provided at the lowermost end of the powder transport conveyor 58. It consists of a phono with a measuring device, ° 84, and 20 kg packaging bags 86 are sequentially carried out by a conveyor.
[ビーズの例〕  [Example of beads]
ブラス ト作業に際しては、 前述のとおり などの熱硬化樹脂で作つたビ一ズを数 種混合する。 これらのビーズ 9 0は、 硬度 (モース) 3. 0〜 4. 5、 比重 1 . :!〜 1 . 5 2、 サイズ 1 0〜 : L 5 0メ ッシュ (約 1 0 0 0〜 : Ι Ο Ο μ πι) で、 図 8 に一例を示すよ う に ( 2 5倍) 、 それぞれ鋭利な稜線をもつ不定形な多面体を なしている。 ただし、 1 0 0 μ m以下 (例えば 5 0 μ m ) でも使用可能である。 所定の空気圧 ( 2〜3 k g / c m 2又はそれ以上の圧力) で噴射されたビ一ズ による剥離を 1 0 mm径ノ ズル 1 本当たり の能力と して示すと、ビーズ噴出量が 1 . 9〜 2. 2 0 k g Zminの場合、 1 m 2当たり剥離時間は、 3〜 6 mi m 2である。 なお、 ビーズの使用 リサイ クル回数は、 圧力によって異なるが、 通常 1 5〜 4 0 回又はそれ以上である。 During blast work, several beads made of thermosetting resin such as those described above are mixed. These beads 90 have a hardness (Mohs) of 3.0-4.5, specific gravity 1.:!~1.52, size 10 ~: L50 mesh (about 10000 ~: Ι Ο Ο) Ομπι), as shown in Fig. 8 (25 times), each forms an irregular polyhedron with sharp edges. However, it can be used even if it is 100 μm or less (for example, 50 μm). When shown as the predetermined air pressure (2~3 kg / cm 2 or more pressure) 1 peeling due injected bi one's at 0 mm径No nozzle 1 capacity per this, beads ejection amount is 1. For 9 to 2.20 kg Zmin, the peel time per m 2 is 3 to 6 mi m 2 . The number of recycles of beads depends on the pressure, but is usually 15 to 40 or more.
上記ビーズの性能は、 一次的には材質 · 硬度 · 比重が特定され、 2次的には切 削性能 · 耐摩耗性 · 耐熱性 · 対静電気特性に優れており 、 3次的にはブラス ト作 業時のス ピー ドが高く 、 粉塵発生割合が少なく 、 再利用性ができ、 ビーズ粉塵そ のものは無公害で一般廃棄物と して扱える、 という ものである。  The performance of the above beads is primarily specified by material, hardness and specific gravity, secondary is excellent in cutting performance, abrasion resistance, heat resistance, anti-static property, and tertiary is blast The work speed is high, the dust generation rate is low, the reusability is high, and the bead dust itself is pollution-free and can be treated as general waste.
次に、 剥離作業の適性条件について説明する。 ①空気圧力 : 0〜 5 kg/ c m 2 ②ノズル径 : 3 、 4、 5 、 6 、 7 、 8 、 8 . 5 1 0 mm Next, suitable conditions for the peeling operation will be described. ①Air pressure: 0-5 kg / cm 2 ②Nozzle diameter: 3, 4, 5, 6, 7, 8, 8.5 8.5 mm
③ビーズと空気の混合比はバルブで調整 ④噴射角度、 距離は剥離対象物の 形態に合わせる。  ③Adjust the mixing ratio of beads and air with a valve. ④Adjust the injection angle and distance to the shape of the object to be peeled.
バンパーチップの剥離は MG— 0、 硬材 (鋼材等) の塗膜 ' 酸化スケール及び 道路標示の剥離には MG— 1 、 塗膜 · サビ ' パリ · 接着剤 · シール ' 床ワ ッ クス などの剥離 · 金属光沢面の防眩 · 壁又は 卜ィ レ等の洗浄には MG— 3または MG 一 5、 軟材 (アルミなど) の塗膜 ' サビ ' バリ . 壁洗浄には MG _ 7、 軟材の塗 膜-床ワ ックス '壁又は トイ レ洗浄に MG— 1 0または MG— 1 4が使用される。  MG-0 for peeling bumper chips, MG-1 for coating hard materials (steel materials) for removing oxide scale and road markings, MG-1 for coating films, rust, Paris, adhesives, seals, floor wax, etc. MG-3 or MG-15 for cleaning of peeling, anti-glare on metallic glossy surfaces, walls or tiles, coating film of soft material (such as aluminum) 'Rust' Burr. MG_7, soft for wall cleaning MG-10 or MG-14 is used for wall coating or floor cleaning.
[試験例 1〕  [Test Example 1]
メ ラ ミ ン樹脂 6 ◦ %とユ リ ァ樹脂 4 0 %の混合材料を加熱加圧して成形した厚 さ 3 m mの樹脂プレー ト状成形物をク ラ ッシャーによ り 3〜 5 m mのサイコ ロ状 に破砕したのち、 上記の装置によって粗砕、 粉砕して 2 0〜 6 5 メ ッシュの剥離 材と し、 これをアルミ缶塗装膜に吹き付けて塗膜を剥離した。  A 3 to 5 mm thick plastic plate-like molded product formed by heating and pressing a mixed material of 6% by weight of melamine resin and 40% of urea resin by a crusher. After being crushed into a batter shape, it was roughly crushed and pulverized by the above-mentioned device to obtain a release material of 20 to 65 mesh, which was sprayed on an aluminum can coating film to peel off the coating film.
6 mm径ノ ズル 1 本当たり の能力は、 空気圧 2 k g c m 2、 ビーズ噴出量 1 .The capacity of one 6 mm diameter nozzle is 2 kgcm 2 air pressure and the amount of beads ejected is 1.
0 k g Zminで、 1 m 2当たり剥離時間 3 niinZ m 2で処理した結果、 5 0 ミ ク ロ ン の塗膜をきれいに剥離して金属アルミ の光沢を現すこ とができた。 0 kg Zmin, 1 m 2 per stripping time 3 niinZ m 2 treated with result, it and this for 5 0 Mi click b down the coating film was released cleanly represent the gloss of the metal aluminum.
〔試験例 2〕  (Test Example 2)
メ ラ ミ ン樹脂プレー トの破砕物 7 0 %とユ リ ァ樹脂プレー 卜の破砕物 3 0 %と を混合し、 これをク ラ ッシャーによ り破砕したのち、 粗砕、 粉砕して 2 0〜 6 5 メ ッシュの剥離材と し、 アルミ缶塗装膜に吹き付けて塗膜を剥離したと ころ、 前 同様塗膜をきれいに剥離するこ とができた。  A mixture of 70% of crushed resin plate and 30% of crushed resin plate was crushed by a crusher, and then crushed and pulverized. As a release material for 0 to 65 mesh, the coating film was peeled off by spraying it onto the aluminum can coating film, and the coating film was successfully removed as before.
〔試験例 3〕  (Test Example 3)
メ ラ ミ ン樹脂とフエノール樹脂の混合材料で成形したプレー ト状樹脂成形物の 破砕物を上記の装置によって破砕し粉砕して 2 0〜 6 5 メ ッシュ剥離材と し、 こ れをスチール缶の 1 0 0 ミ ク ロ ン塗装膜に吹き付けて塗膜を剥離した。 6 mm径ノ ズル 1 本当たりの能力は、 空気圧 3 k g / c m 2、 ビーズ噴出量 1 . O k g Zmin で、 1 m 2当たり剥離時間 3 minZm 2で処理した結果、 塗膜をきれいに剥離して 金属光沢を現すことができた。 産業上の利用可能性 A crushed plate-like resin molded product molded from a mixed material of a melamine resin and a phenol resin is crushed and crushed by the above-mentioned equipment to obtain a mesh release material of 20 to 65, which is used as a steel can. The coating film was peeled off by spraying on the 100 micron coating film. 6 mm径No capacity per one nozzle is, the air pressure 3 kg / cm 2, a bead ejection amount 1. O kg Zmin, 1 m 2 per stripping time 3 result treated with MinZm 2, and cleanly peeled coating film A metallic luster could be exhibited. Industrial applicability
上記のよ うに、 本発明は、 製造工程では粗碎部で粗砕したのち、 数段階の粉碎 ロールによ り粉砕し篩分けするこ とで、 ワーク加工の目的に適応する分級段階ご とに粒度が均質化された研削又は剥離用ビーズを容易に製造することができ、 特 に、 粉砕ロールの形状 (凹凸ピッチ、 対向ロールのク リ アランス) を重要視し、 各種ワークの研削 · 研掃や瞬間剥離に適する不定形な多面体のビーズを提供する こ とができる。 粉砕ロールの形状を選択するこ とによ り ビーズ粒径の変更、 調整 が容易となり、 粉碎加工時における粉塵や騒音の発生が少なく 効率的にビーズを 製造するこ とができる。 また、 ビーズサイズの粒度均質化によ り研削 · 剥離能が 向上し、 瞬間剥離などの作業時間の短縮をはかることができる。 さ らに、 剥離対 象品 (ワーク) を傷つけず、 例えば、 アルミ缶、 スチール缶、 自動車バンパー等 の塗膜を剥離して不用品を再生するなどの剥離作業に有用なビーズを効率的に製 造することが可能である。  As described above, in the present invention, the present invention is characterized in that in the production process, after crushing in a crushing section, crushing and sieving are performed by several stages of crushing rolls, so that the crushing is performed at each classification step adapted to the purpose of work processing. Grinding or peeling beads with a uniform particle size can be easily manufactured. In particular, emphasis is placed on the shape of the crushing roll (concavo-convex pitch, clearance of the opposing roll), and grinding and polishing of various workpieces. In addition, irregular polyhedral beads suitable for instantaneous peeling can be provided. By selecting the shape of the crushing roll, it is easy to change and adjust the bead particle size, and it is possible to efficiently produce beads with less generation of dust and noise during the crushing process. In addition, the homogenization of the particle size of the beads improves the grinding and peeling ability, and can shorten the work time for instantaneous peeling and the like. Furthermore, beads that are useful for peeling work such as peeling off coatings on aluminum cans, steel cans, automobile bumpers, etc., and regenerating non-consumables can be efficiently used without damaging the peeled product (work). It can be manufactured.

Claims

請 求 の 範 囲 The scope of the claims
1 . 熱硬化性樹脂成形物の粒径 1 0 0 0〜約 5 0 μ m範囲の粉砕物で、 各粒子が 実質的に鋭利な稜線を持つ不定形な多面体と され、 かつ分級段階ごとに粒度がほ ぼ均質化されているこ とを特徴とする研削用ビーズ。 1. Pulverized product of thermosetting resin molded product having a particle size in the range of 100 to about 50 μm, each particle being an irregular polyhedron with a sharp ridge line, and for each classification step Grinding beads characterized in that the particle size is almost uniform.
2 - 熱硬化性樹脂成形物は、 メ ラ ミ ン、 ユ リ ア、 フユノール、 不飽和ポリエステ ル、 アク リル、 グアナミ ン、 エポキシ及びポリ ウレタンから選ばれた 1種または 2種以上である請求項 1記載のビーズ。  2-The thermosetting resin molded product is one or more selected from melamine, urine, fuynol, unsaturated polyester, acryl, guanamine, epoxy and polyurethane. Beads according to 1.
3 . 熱硬化性樹脂成形物は、 メ ラ ミ ン、 ユリ ア及びノ又はフ ノール樹脂の混合 物である請求項 1 記載のビーズ。  3. The beads according to claim 1, wherein the thermosetting resin molded product is a mixture of a melamine, a urine, and a phenolic or phenolic resin.
4 . 熱硬化性樹脂の成形材料調製に先立つ樹脂素材の混合段階で、 パルプ及びガ ラス繊維布細片を充填し、 さ らに熟成、乾燥後の混合段階でカーボン、人造黒鉛、 金属紛又は金属繊維と着色材を配合してなる請求項 1 記載のビーズ。  4. Fill the pulp and glass fiber cloth at the mixing stage of the resin material prior to the preparation of the molding material of the thermosetting resin, and further ripen and dry the carbon, artificial graphite, metal powder or The bead according to claim 1, wherein a metal fiber and a coloring material are blended.
5 . 熱硬化性樹脂の成形材料調製に先立つ樹脂素材の混合段階で、 パルプ及びガ ラス繊維布細片を充填し、 さ らに熟成、乾燥後の混合段階でカーボン、人造黒鉛、 金属紛又は金属繊維と着色材を配合してプレー ト状樹脂成形物を作り、 この樹脂 成形物をサイ コ ロ状ないしペレツ 卜状に破砕したのち、 向かい合う ロール表面の 凹凸が 1 2 ピッチの位相ズレをもって形成された多段式の粉碎ロールによって、 熱硬化性樹脂成形物の粗砕物を粒径 1 0 0 0〜約 5 0 μ mに粉砕するこ とによ り、 各粒子が実質的に鋭利な稜線を持つ不定形な多面体微細物とすることを特徴とす る研削用ビーズの製造方法。  5. Fill the pulp and glass fiber cloth pieces in the mixing step of the resin material prior to the preparation of the molding material of the thermosetting resin, and further ripen and dry the carbon, artificial graphite, metal powder or A plate-shaped resin molded product is made by blending metal fibers and a coloring material, and this resin molded product is crushed into a cyclo-like or pellet-like shape, and the concavities and convexities on the facing roll surface are formed with a phase shift of 12 pitches The crushed material of the thermosetting resin molded product is crushed to a particle size of 100 to about 50 μm by the multi-stage crushing rolls, so that each particle has a substantially sharp ridge line. A method for producing beads for grinding, characterized in that it has an amorphous polyhedral fine material.
6 . 重合凝縮後の熱硬化性樹脂素材中に、 パルプ 3 0〜 4 0 %、 ガラス繊維布細 片 0 . 1 〜 0 . 5 %を配合し、 同樹脂の熟成乾燥後に静電気発生抑制と帯電抑制 のため炭素粉または導電率 0 . 2 〜 0 . 3の人造黒鉛と、 比重を 1 . 8以上に上 昇させるために金属紛又は金属繊維 0 . 1 〜 0 . 5 %を配合させてなる請求項 5 記載のビーズの製造方法。  6. 30 to 40% of pulp and 0.1 to 0.5% of glass fiber cloth flakes are blended into the thermosetting resin material after polymerization condensation. Carbon powder or artificial graphite with electrical conductivity of 0.2 to 0.3 for control, and metal powder or metal fiber of 0.1 to 0.5% for raising the specific gravity to 1.8 or more A method for producing the beads according to claim 5.
7 . プレー ト状樹脂成形物は、 メ ラ ミ ン、 ユ リ ア、 フエ ノ ール、 不飽和ポリ エス テル、 アク リル、 グアナミ ン、 エポキシ及びポリ ウレタンから選ばれた 1 種また は 2種以上からなる請求項 5または 6記載のビーズの製造方法。  7. The plate-like resin molded product is one or two selected from melamine, urine, phenol, unsaturated polyester, acryl, guanamine, epoxy and polyurethane. 7. The method for producing beads according to claim 5, comprising the above.
16 16
訂正された用紙 (規則 91 ) Corrected form (Rule 91)
8 . ブレー 卜状樹脂成形物は、 メ ラ ミ ン、 ユリ アまたはフエ ノ ール樹脂の混合物 である請求項 7記載のビーズの製造方法。 8. The method for producing beads according to claim 7, wherein the braided resin molded product is a mixture of a melamine, a urine or a phenolic resin.
9 . プレー ト状樹脂成形物は、 メ ラ ミ ン樹脂 7 0 〜 8 0 %にユリ ア樹脂 3 0 〜 2 0 %を配合したことを特徴とする請求項 8記載のビーズの製造方法。  9. The method for producing beads according to claim 8, wherein the plate-like resin molded product is obtained by mixing 30 to 20% of a urea resin with 70 to 80% of a melamine resin.
1 0 . メ ラ ミ ン、 ユ リ ア、 フエ ノール、 不飽和ポリ エステル、 アタ リ ノレ、 グアナ ミ ン、 エポキシ及びポリ ウ レタンから選ばれた 2種以上の成形材料でそれぞれ成 形されたプレー ト状樹脂成形物を、 各成形物ごとに破砕したのち混合して粉砕す るこ とからなる請求項 5記載のビーズの製造方法。  10. A plastic molded with at least two molding materials selected from the group consisting of melamine, urine, phenol, unsaturated polyester, ataline, guanamine, epoxy and polyurethane. 6. The method for producing beads according to claim 5, comprising crushing the resin-like resin molded products for each molded product, followed by mixing and crushing.
1 1 . プレー ト状メ ラ ミ ン樹脂成形物とプレー ト状ユ リ ァ樹脂成形物を、 それぞ れサイ コ ロ状ないしペレッ ト状に破砕したのち、 前者を 6 0 〜 7 0 %、 後者を 4 0 〜 3 0 %の割合に混合して粉砕するこ とを特徴とする請求項 1 0記載のビーズ の製造方法。  11 1. After crushing the plate-shaped resin resin molded product and the plate-shaped resin molded resin material into the shape of a cyclo or pellet, respectively, the former is 60 to 70%, The method for producing beads according to claim 10, wherein the latter is mixed at a ratio of 40 to 30% and pulverized.
1 2 .熱硬化性樹脂のプレー 卜状成形物をほぼ 2 m m角に粗砕する粗砕ロールと、 粗砕口一ルによって得た粗砕物を、 粒径 1 0 0 0〜約 5 0 μ ΐΏで鋭利な稜線を持 つ不定形な多面体に粉砕すべく 、 向かい合う ロール表面の凹凸が 1 2 ピッチの 位相ズレをもつて形成された多段式の粉砕口ールとを備えたこ とを特徴とする研 削用ビーズの製造装置。  12.The crushing roll for crushing the plate-like molded product of thermosetting resin into approximately 2 mm square, and the crushed material obtained by the crushing nozzle, with a particle size of 100 to about 50 μm In order to pulverize into an irregular polyhedron with a sharp ridgeline, a multi-stage pulverizer is formed, in which the concavities and convexities on the opposing roll surfaces are formed with a phase shift of 12 pitches. Production equipment for polishing beads.
1 3 . 熱硬化性樹脂材料のプレー ト状成形物をサイ コ口状ないしペレツ 卜状に破 碎するク ラ ッシャー咅 15と、  1 3. Crusher No. 15 for crushing a plate-like molded product of thermosetting resin material into a shape like a mouth or a pellet,
クラ ッシャ一部で破砕された破砕物中の金属 · 異物類除去する選別部と、 選別部を経たサイ コ ロ状ないしペレツ 卜状破砕物を約 2 m m角に粗砕すべく 、 ロール表面に 1 2 ピッチ位相ズレの凹凸が形成された一対の破砕ロールを具え た粗砕部と、  A sorting unit that removes metal and foreign matter in the crushed material crushed by a part of the crusher, and a roll or pellet-like crushed material that has passed through the sorting unit 1 2 A crushing unit equipped with a pair of crushing rolls with irregularities of pitch phase shift,
粗砕部で得た粗砕物を、 実質的に鋭利な稜線をもつ不定形な多面体で粒径ほぼ 1 0 0 0〜約 5 0 μ mに粉碎すべく 、 前記破砕ロールと同様口ール表面に 1 / 2 ビッチ位相ズレの凹凸が形成された粉砕ロール対を多段式に具えた粉碎部と、 前記粉砕部の下流に配置されて、 粉砕されたビーズ粒径を分級段階ごとにほぼ 均一化する分級装置と、 からなる剥離用ビーズの製造装置。  Similar to the crushing roll, the crushed material obtained in the crushing section is crushed into an irregular polyhedron having substantially sharp ridges to a particle size of approximately 100 to approximately 50 μm. A crushing unit equipped with a multi-stage crushing roll pair having irregularities with 1 / 2-bit phase shift, and placed downstream of the crushing unit to make the particle size of the crushed beads almost uniform at each classification stage And a separation bead manufacturing device.
1 4 . 熱硬化性樹脂のプレー ト状成形物を約 2 〜 4 m m角の不定形物なサイ コ 口 状ないしペレツ ト状に破砕するクラ ッシャ一部と、 .' ク ラッシャ一部で破砕された破砕物中の金属 · 異物類除去する選別部と、 一対のロール表面に 1 / 2 ピッチの位相ズレをもつ凹凸が形成されて選別部で 選別された破砕物を粗砕する少なく と も一対の破砕ロールと静電気除去装置を具 えた粗砕部と、 14. A thermoformed resin plate-like molded product is an irregular shape of about 2 to 4 mm square. A part of the crusher that crushes into a shape like a pellet, a separator that removes metal and foreign matter in the crushed material crushed by the part of the crusher, and a phase shift of 1/2 pitch between the pair of roll surfaces A crushing unit provided with at least one pair of crushing rolls and a static eliminator for crushing the crushed material selected in the sorting unit by forming irregularities having
粗砕部で得た粗砕物を、 実質的に鋭利な稜線をもつ不定形な多面体で粒径ほぼ 1 0 0 0〜約 5 0 μ mに粉砕すベく 、 前記破砕ロールと同様口ール表面に 1 / 2 ピッチの位相ズレをもつ凹凸が形成された多段式粉砕ロール対と静電気除去装置 を具えた粉砕部と、  The crushed material obtained in the crushing section is crushed into an irregular polyhedron having substantially sharp ridges to a particle size of approximately 100 to approximately 50 μm. A pulverizing unit equipped with a multi-stage pulverizing roll pair having irregularities having a phase shift of 1/2 pitch on the surface and a static eliminator,
前記粉砕部の下流に切替弁を設けて配置された微細粒のビーズを分級する風力 分級機及び微細粒よ り大径粒のビーズを分級する電力分級機と、  An air classifier for classifying fine-grained beads and a power classifier for classifying finer-sized beads than the fine-grained beads arranged with a switching valve downstream of the pulverizing section;
風力分級機または電力分級機によって分級されたビーズを計量、 袋詰、 自動縫 装によ り、 所定容量の剥離用ビーズ包装品とする包装出荷部とからなり、  The packaging and shipping department consists of weighing, bagging, and automatic sewing of beads classified by an air classifier or an electric power classifier to make a predetermined volume of peeled bead packaging.
しかも、 前記風力分級機と電力分級機のメ ッシュ上の細粒物を選別部の上流又 は粗砕部の上流に リ ターンさせる循環ライ ンと、 ク ラ ッシャー部から分級機まで の各段階で生じる微細粒を含む粉塵を粉塵処理装置に導く ダク 卜 とを具えている こ とを特徴とする ビーズの製造装置。  In addition, a circulation line for returning the fine particles on the mesh of the air classifier and the power classifier upstream of the sorting section or upstream of the crushing section, and each stage from the crusher section to the classifier. And a duct for guiding the dust containing fine particles generated in the step to a dust treatment device.
1 5 . 破砕ロールの凹凸ピッチ及び対向ロール間のク リ アランスを最適なものに 設定するこ とでビーズ粒径の変更、調整を行う粒度調整機構を具えた請求項 1 2 、 1 3 または 1 4記載のビーズの製造装置。  15. A particle size adjusting mechanism for changing and adjusting the bead particle size by setting the unevenness pitch of the crushing roll and the clearance between the opposing rolls to be optimal. An apparatus for producing beads according to 4.
1 6 . 前記分級装置は、 前記粉砕機によって粉砕されたビーズを分級すべく 、 順 次編み目を細かく した数段の篩い網を有する振動篩い機と、 各篩い網上にあたる 篩い機外壁から導出したシュー ト と、 各シュー トに接続したダク ト又はコンペャ とから構成され、 第 1段メ ッシュアップのものは前記粉砕機に送られて再度粉砕 され、 最下段メ ッシュアンダーは粉塵と して廃棄され、 第 2段以下の中間段メ ッ シュ上のものはフ レコン詰め機又は 2 0キロ袋詰め機に送られて計量、 袋詰めさ れて順次搬出されるよ うにされている請求項 1 4または 1 5に記載のビーズ製造 装置。  16. The classifying device was derived from a vibrating sieve having several stages of sieve meshes in order to classify beads crushed by the crusher, and a sieve outer wall corresponding to each sieve mesh. It consists of a shoot and a duct or a conveyor connected to each shoot.The first-stage mesh-up is sent to the crusher and crushed again, and the lower-most mesh under is discarded as dust. Claim 14 or Claim 14 wherein the items on the second and lower intermediate meshes are sent to a frecon packing machine or a 20kg bagging machine, weighed, bagged, and sequentially carried out. 15. The bead production apparatus according to 15.
PCT/JP2000/000516 1999-02-01 2000-01-31 Grinding beads and beads production method and device therefor WO2000045994A1 (en)

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CN111550986A (en) * 2020-05-12 2020-08-18 范智锋 Drying all-in-one is smashed to chinese-medicinal material
CN115318803A (en) * 2022-08-31 2022-11-11 安徽国伟金属资源有限公司 Circuit board is retrieved and is used broken separator
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