WO2006109422A1 - Procede d’elaboration d’un produit pulverise, appareil et produit pulverise - Google Patents
Procede d’elaboration d’un produit pulverise, appareil et produit pulveriseInfo
- Publication number
- WO2006109422A1 WO2006109422A1 PCT/JP2006/305397 JP2006305397W WO2006109422A1 WO 2006109422 A1 WO2006109422 A1 WO 2006109422A1 JP 2006305397 W JP2006305397 W JP 2006305397W WO 2006109422 A1 WO2006109422 A1 WO 2006109422A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- grinding
- pulverized
- grinding surface
- ground
- pulverized product
- Prior art date
- Legal status (The legal status 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 status listed.)
- Ceased
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/02—Crushing or disintegrating by disc mills with coaxial discs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/11—Details
- B02C7/12—Shape or construction of discs
- B02C7/13—Shape or construction of discs for grain mills
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/11—Details
- B02C7/17—Cooling or heating of discs
Definitions
- the present invention relates to a method, an apparatus, and a pulverized product for producing a pulverized product by pulverizing food materials such as wheat, rice, buckwheat, and soybean, and other pulverized products, in particular, granular pulverized products. More specifically, the present invention relates to a method, an apparatus, and a pulverized product for producing a pulverized product having a uniform particle size by grinding the surface of the pulverized product particle by a pair of pulverizers arranged opposite to each other. It is.
- Food raw materials such as living organisms, organic substances, chemical substances, and other materials to be pulverized to produce pulverized materials.
- raw material to be crushed such as food is supplied between a pair of pulverizers arranged opposite to each other, and the pulverized material is pulverized between the pulverizers by rotating at least one of the pulverizers.
- the grinding surface of the stone mill is formed with a groove in the radial direction from the center side, and the material to be crushed is supplied between the grinding machines from the raw material supply unit provided at the eccentric position on the center side. It is configured to coarsely pulverize on the side, and sequentially send it to the peripheral side and finely pulverize on the peripheral side.
- cereal particles such as wheat, buckwheat, and soybean have a soft thin epidermis on the surface, but when cereal particles having such a soft thin film are pulverized, the high endosperm part and the like are finely pulverized.
- the soft thin film portion is not finely pulverized and is taken out from the peripheral portion side by rubbing between the pulverizers with a large particle size.
- a crusher rotating type crusher When a crusher rotating type crusher is rotated at a high speed, the raw material is heated and oxidized. The components are altered, and the quality of the obtained pulverized product such as aroma, flavor and texture is lowered.
- a pulverizer rotating type pulverizer is configured such that one pulverizer is rotated by a drive device, and the drive-side pulverizer rotates and its drive mechanism is complicated, so the drive side is cooled. It is difficult to do.
- the pulverizer on the opposite side that is, the fixed side can be easily cooled, but it is difficult to prevent the pulverized product from being deteriorated due to the cooling effect on the pulverizer on the rotating side.
- An object of the present invention is to break down a soft thin film efficiently and finely pulverize it with a simple apparatus and operation, even when pulverizing an object having a soft thin film such as cereal particles. It is also possible to provide a method for producing a pulverized product, an apparatus, and a pulverized product, which can obtain a pulverized product of fine particles having a uniform particle size.
- the present invention provides the following pulverized product production method, apparatus and pulverized product.
- a pair of grinding machines having a grinding surface at the center and a grinding surface at the periphery are opposed to form a grinding part and a grinding part between the opposing surfaces
- the surface of the supplied particles to be crushed is ground and coarsely pulverized in the grinding part, and the ground and coarsely pulverized coarsely pulverized substance is pulverized in the pulverizing part.
- a method for producing a pulverized product is a method for producing a pulverized product.
- At least one of the grinding surfaces has a reverse grinding surface on the center side that is lower than the reference grinding surface on the grinding surface side, and the ground force on the reverse grinding surface extends toward the periphery of the reference grinding surface.
- a grinding part that has a grinding surface in the central part and a grinding surface in the peripheral part, grinds the surface of the particles to be ground in the grinding part between the opposing surfaces, and coarsely pulverized coarsely pulverized substance.
- a raw material supply unit for supplying the material to be ground to the grinding unit
- a pulverized product take-out unit for removing the pulverized product from the pulverization unit
- An apparatus for producing a pulverized product An apparatus for producing a pulverized product.
- At least one of the grinding surfaces has a reverse grinding surface on the center side that is lower than the reference grinding surface on the grinding surface side, and the ground force on the reverse grinding surface extends toward the periphery of the reference grinding surface
- the material to be crushed is not limited as long as it can be pulverized, but is not limited to food materials such as wheat, rice, buckwheat, and soybeans, and other materials such as organisms, organic substances, and chemical substances. Can be mentioned.
- the surface is soft like wheat, buckwheat and soy. Thin, cereal grains having an epidermis, and other particles having a soft thin film are not limited to these.
- a pulverized material production apparatus for use in the pulverized material production method of the present invention has a grinding surface at the center and a pulverized surface at the periphery, and the surface of the pulverized material particles is ground between the opposing surfaces.
- a pair of pulverizers that form a grinding part that performs grinding and coarse pulverization, and a pulverization part that shears and pulverizes the coarsely pulverized coarsely pulverized product, and a drive device that rotates at least one of the pulverizers.
- the apparatus for producing a pulverized product includes a raw material supply unit that supplies the pulverized product to the grinding unit and a pulverized product take-out unit that extracts the pulverized product from the pulverization unit.
- the pair of pulverizers is formed into a disk shape from iron or other metal. It is preferably formed in a disc shape, but other shapes may be used.
- the opposing surfaces of the pair of grinding machines each have a grinding surface at the center and a grinding surface at the periphery. Thereby, when these pulverizers are made to face each other, a grinding part is formed in the central part by the grinding surface between the opposing surfaces, and a pulverization part is formed in the peripheral part by the pulverization surface. If a roughened surface is formed on the further peripheral portion of the pulverized surface, it can be further finely pulverized.
- the grinding surface of at least one of the pulverizers is preferably formed in a stepped shape so as to have a reverse grinding surface on the central side that is lower than the reference grinding surface on the pulverizing surface side. In this case, it is preferable to form an object passage on the reference grinding surface that extends toward the peripheral portion of the reference grinding surface from the reverse grinding surface side.
- the reverse grinding surface may be formed in a plurality of steps.
- the surface of the metal die is etched by blasting or the like by causing the abrasive particles to collide with the object at high speed.
- a rough surface processed portion can be formed.
- Wet (wet) blasting which is a cold process in which media such as abrasives are mixed with liquid (water), or dry blasting, which is a hot process in which media such as abrasives are directly blown with air Either of these may be used, but in order to obtain a pulverized product of ultrafine powder, etching by wet blasting is desirable.
- wet blasting which is a cold process in which media such as abrasives are mixed with liquid (water)
- dry blasting which is a hot process in which media such as abrasives are directly blown with air Either of these may be used, but in order to obtain a pulverized product of ultrafine powder, etching by wet blasting is desirable.
- the force determined by the particle size of the pulverized product is generally 0.005 to 2 mm, preferably 0.01 to 0.2 mm.
- the distance between the grinding surfaces of the grinding part on the center side can be configured to be a force determined by the particle size of the material to be crushed, generally 0.5 to 20 mm, preferably 1 to 10 mm.
- the distance between the reverse grinding surfaces is determined by the particle size of the material to be crushed and is generally 0.2 to 2 mm, preferably 0.5 to lmm. Can be configured.
- Each of the above-mentioned intervals may be the same interval throughout the entire area, but may be narrowed in accordance with the central side force and the peripheral side side.
- the grinding surface that forms the grinding part grinds the surface of the particles to be crushed, breaks a soft thin film such as a soft thin skin formed on the surface, or cracks, and It is comprised so that all or one part of particle
- the grinding surface can be formed integrally with the material constituting the pulverizer, but is preferably composed of a material having higher hardness than the material constituting the pulverizer. Examples of such a grinding surface include those having an abrasive layer containing abrasive grains such as diamond particles, CBN (boron nitride) particles, and WA (white acid-alumina) particles.
- diamond particles, CBN particles, WA particles and other abrasive grains are preferably electrodeposited or non-electrodeposited with a metal such as Ni, and those having a fixed layer force fixed to the ground surface by other fixing materials.
- the particle size of abrasive particles such as diamond particles, CBN particles and WA particles is 0.005 to 0.5 mm, preferably 0.05 to 0.4 mm, and the thickness of the adhesive layer such as a mesh layer is 0.005. It is preferable that the fixed layer is formed so that these particle particles are irregularly shaped and protrude in the form of sandpaper, preferably 0.3 mm, preferably 0.25 mm to 0.25 mm.
- the upper surface of the ground surface on which the abrasive layer is formed may be the same surface as the pulverized surface or may be continuous in an inclined shape.
- the fixed layers of the reverse grinding surface and the reference grinding surface may be the same or different. If they are different, it is preferable that the reverse grinding surface has a coarser grain size than the reference grinding surface.
- the particle size of the abrasive particles on the reverse grinding surface is preferably larger than the particle size of the abrasive particles on the reference grinding surface.
- the grinding object path formed on the reference grinding surface is the force on the reverse grinding surface side
- the back grinding surface side communicates at a depth close to the reverse grinding surface
- the peripheral side is reference grinding It is preferably a deep groove extending in a circular arc shape or a radial shape so that the width and depth gradually decrease toward the tip side slightly before the peripheral portion of the surface.
- the pulverized material passage is a smooth groove without forming a ground surface by abrasive particles or the like.
- the grinding surface formed in the peripheral part of the grinding machine preferably has arcuate grooves extending radially from the central side (grinding part side) to the peripheral side.
- This arc-shaped narrow groove is an arc shape (a spiral formed when particles are radiated in all directions from the center of rotation), which almost coincides with the flow of fine powder observed on the grinder as the grinder rotates. That are grooves) are preferred.
- the arc shape means a shape similar to an arc such as an arc, an ellipse, or a spiral.
- the arc-shaped narrow groove formed on the ground surface has a width of 0.01-0.5 mm, preferably 0.05-0.3 mm, a depth of 0.05-lmm, preferably 0.1-0.3 mm. Yes, it can be formed by mechanical processing such as milling machine, energy beam processing such as laser processing and water jet processing, and other processing methods.
- the arcuate fine grooves on the grinding surface of at least one of the grinding machines are preferably laser processed grooves.
- a pair of pulverizers are formed in substantially the same shape except that they have different configurations as described above, and are used as a pulverizer pair by superimposing them. At this time, the circular arc-shaped grooves formed on the grinding surface of the grinding part are overlapped in the intersecting direction.
- Such a pair of grinders can be arranged in an arbitrary direction such as a vertical direction, a horizontal direction, or an oblique direction. In particular, it is preferable to arrange in the longitudinal direction or in an oblique direction close to the longitudinal direction because the pulverized material can be easily taken out.
- one of the pulverizers is connected to the drive unit to make it a rotary type. If the other pulverizer is fixed and not rotated, the arrangement of the cooling section and the raw material supply section is facilitated.
- the raw material supply unit may be connected to a pulverizer that is not connected to the driving device (fixed type), and the pulverized material may be supplied to the grinding unit through the pulverizer.
- the connection position of the raw material supply unit can be the central part of the fixed crusher, but it may be eccentric.
- the pulverized material take-out part is provided in the peripheral part of the pulverizer, but an annular passage is provided along the periphery of the pulverizer, It is possible to rotate the scraping pieces provided in the peripheral part of the rotary crusher in the annular passage to collect the pulverized material and to take out the pulverized material takeout force.
- the pulverizer becomes high temperature due to frictional heat due to rotation, and therefore can be configured to be cooled by a cooling unit.
- each pulverizer is cooled by a cooling unit provided adjacent to each other.
- the rotary pulverizer is difficult to seal with the water-cooled type, if the compressed gas is cooled by adiabatic expansion of the compressed gas, the gas can be introduced into the grinding part and the pulverization part to cool the object to be crushed and the pulverized object. Therefore, it is preferable.
- the gas air is inexpensive, but an inert gas may be used.
- the stationary pulverizer can be sealed, for example, by water cooling, by passing a refrigerant through the jacket.
- the cooling temperature by adiabatic expansion cooling is 10 to -30 ° C, preferably 0 to -5 ° C
- the cooling temperature by cooling the refrigerant is 10 to -30 ° C, preferably 0 to -20 ° C. This is preferable because it prevents condensation due to adiabatic expansion cooling of the compressed gas, cools the pulverized material and pulverized material, and prevents quality deterioration.
- a grinding part and a pulverization part are formed between opposing pulverization surfaces of a pair of pulverization machines by the above-described apparatus, and one of the pulverization machines is rotated by a driving device. Then, the raw material is supplied from the raw material supply unit to the grinding unit, and the surface of the supplied particles to be ground is ground in the grinding unit and coarsely pulverized.
- the pulverized product is produced by cutting, crushing and pulverizing, and taking out the pulverized product from the pulverization unit to the pulverized product take-out unit.
- the surface of the particles to be ground is ground by the grinding surface by the rotation of the grinding machine, and the soft thin film such as the soft thin skin formed on the surface is broken or cracked.
- the whole or part of the particles to be crushed is coarsely pulverized.
- a grinding surface having an abrasive layer containing abrasive grains such as diamond particles, CBN particles, and WA particles
- the irregularly shaped particles protruding from the grinding surface force pierce the thin film and easily break.
- the to-be-ground material particles between the grinding surfaces are coarsely pulverized in whole or in part by the rotation of one of the pulverizers, which facilitates pulverization in the pulverization unit.
- the distance between the reverse grinding surfaces (the opposing surface is not the reverse grinding surface) May be larger than the gap between the reference grinding surfaces, so that coarse pulverization of large particle size particles occurs in this portion, and coarse pulverization of small particle size particles occurs between the reference grinding surfaces.
- the grinding object passage is formed on the reference grinding surface, large-sized particles move from the reverse grinding surface side to the periphery of the reference grinding surface, and are coarsely pulverized and moved between the reference grinding surfaces. Small particle size.
- the reverse grinding surface side is connected at almost the same depth as the reverse grinding surface, and the peripheral side is arc-shaped with a gradually decreasing width and depth toward the tip, slightly before the peripheral part of the reference grinding surface.
- the ground material passage is preferably formed as a smooth concave groove without forming a ground surface by abrasive particles or the like, so that blockage in the ground material passage can be prevented.
- the coarsely pulverized material ground and coarsely pulverized in the grinding part is sheared between the pulverized surfaces, crushed and pulverized to form a pulverized product with a small particle size.
- soft thin films such as thin skins that are broken or cracked in the grinding part are also crushed to a small particle size by shearing and crushing between the pulverized surfaces, and the whole is pulverized to a uniform small particle size. It becomes a thing.
- the grinding surface has arcuate grooves extending radially from the center side (grinding part side) to the peripheral side
- the arcuate grooves increase the shearing and crushing effect and increase crushing efficiency.
- circular narrow grooves by energy beam carriage such as laser processing and water jet processing have a sharp edge and thus have a large shearing and crushing effect.
- the object to be pulverized and the pulverized object can be cooled, thereby preventing deterioration of quality.
- a cooling unit provided adjacent to each crusher as the cooling unit, cooling suitable for each crusher can be performed.
- a rotating pulverizer is preferable when cooled by adiabatic expansion of compressed gas, because it is possible to cool the material to be crushed and the pulverized material by introducing the gas into the grinding and pulverizing portions without the need to tighten the seal.
- the fixed crusher can be cooled to a low temperature with a simple device and operation by passing a coolant through the jacket and sealing it with a water-cooled type, for example.
- the powdered material is taken out to the powdery material extraction part from the powdery board powdery part.
- the powder take-out part is provided in the peripheral part of the powder grinder, but if an annular passage is provided along the periphery of the grinder and a grind piece is provided in the peripheral part of the rotary grinder, the rotary type of the grinder.
- the scraper piece in the annular passage By rotating, the pulverized material can be collected and collected, and the pulverized material takeout force can be taken out. In this case, the removal of the pulverized material can be promoted by introducing the cooling gas into the annular passage.
- the pulverized product of the present invention is a pulverized product obtained by the above method, and even when it has a soft thin film such as cereal particles, fine particles having a uniform particle size as a whole can be obtained.
- the processed product of the present invention is a processed product containing the above finely pulverized product, and an excellent quality processed product can be obtained by using fine particles having a uniform particle size as a whole.
- a seed coat portion rich in fragrance components, nutrient components, and enzyme activities can be pulverized at a low temperature, so that it is excellent in fragrance and flavor and has a high nutrient component content.
- High quality pulverized products, processed raw materials and processed products can be manufactured.
- the pulverized product, processed raw material, and force product obtained by the method of the present invention have good enzyme activities such as a-amylase and GOT (glutamate oxalate acetate transaminase), the dry chemistry method is used.
- a-amylase and GOT glycoxalate acetate transaminase
- a pair of grinding machines having a grinding surface at the center and a grinding surface at the periphery are opposed to each other, and a grinding part and a grinding part are formed between the opposing surfaces.
- the apparatus rotates at least one of the pulverizers, supplies the material to be ground from the raw material supply unit to the grinding unit, and grinds the surface of the supplied particles to be ground in the grinding unit and coarsely pulverizes them.
- the pulverized coarsely pulverized product is sheared, crushed and pulverized in the pulverizing unit, and the pulverized product is taken out from the pulverizing unit, so that it has a soft thin film like cereal particles by simple equipment and operation. Even when the material to be pulverized is pulverized, the soft thin film can be efficiently broken to be finely pulverized, whereby a finely pulverized fine particle pulverized material can be obtained.
- Fig. 1 is a longitudinal sectional view showing the pulverized product production apparatus of Example 1
- Fig. 2 is a front view of the pulverizer 2, viewed from the upper left side of Fig. 1
- Fig. 3 is a rear view thereof. It is the figure seen from the lower right side.
- the pulverized product manufacturing apparatus 1 has a pair of pulverizing discs 2 and 3 arranged to face each other in an inclined manner.
- One crusher 2 is connected to a driving device M and is a rotary type.
- the other crusher 3 is fixed and connected to the raw material supply unit 4.
- the pulverizers 2 and 3 have grinding surfaces 2a and 3a at the central portion and pulverizing surfaces 2b and 3b at the peripheral portion, respectively, and a grinding portion 5 and a pulverizing portion 6 are formed between the facing surfaces.
- the grinding surface 3a of one crusher 3 is entirely formed on the same surface, but the grinding surface 2a of the other crusher 2 is back ground with lower than the reference grinding surface 2c on the crushing surface 2b side.
- An arc-shaped, radial deep groove 2e is formed as a stepped shape so as to have the surface 2d on the center side, and extends from the reverse grinding surface 2d side toward the peripheral portion of the reference grinding surface 2c.
- the reference grinding surface 2c is formed so that the width and depth gradually decrease toward the tip side.
- an abrasive layer 7 in which abrasive grains such as diamond particles are fixed by electrodeposition of a metal layer (Ni plating). However, it is formed in the deep groove 2e.
- the crushing surfaces 2b and 3b formed in the peripheral part of the crushing machines 2 and 3 are formed with arc-shaped narrow grooves 2f and 3f extending radially on the center side (grinding part 5 side) force peripheral side. .
- These arc-shaped narrow grooves 2f and 3f are arc-shaped (particles are radiated in all directions from the center of rotation) which almost coincides with the flow of fine powder observed on the grinding machines 2 and 3 as the grinding machine 2 rotates. It is a spiral groove that is sometimes formed.
- the arcuate narrow groove 2f of the crusher 2 is formed by laser processing.
- the grinding surface 3a of the crusher 3 is entirely formed on the same surface in the same manner as the reference grinding surface 2c of the grinding surface 2a, and no reverse grinding surface is formed, but the center of the grinding surface 3a is not formed.
- the raw material supply unit 4 is connected to the unit.
- the arcuate narrow groove 3f of the crusher 3 may be formed by force laser processing that is formed in an arcuate narrow groove in the same direction as the arcuate fine groove 2f of the crusher 2 by milling.
- the pair of pulverizers 2 and 3 may have almost the same shape except that they have different configurations as described above. Therefore, when these are overlapped to form a pulverizer pair,
- the arcuate grooves 2f and 3f formed on the grinding surfaces 2b and 3b are overlapped in the intersecting direction.
- a drive pin hole 8 is formed on the back surface of the pulverizer 2 so that the drive pin 9 of the drive device M can be engaged and rotated.
- a cooling spiral groove 11 is formed on the back of the crusher 2 so as to reach the peripheral side of the central force.
- the protruding members 12a and 12b are configured to face each other.
- the cooling gas ejection members 12 a and 12 b are attached to the gantry 13 and communicate with the compressed gas generator 14.
- a grind piece 15 is attached to the outer peripheral surface of the crusher 2 by a mounting member 16, and is rotated by an annular passage 17 formed along the periphery of the crusher 2. It is configured to be taken out from the pulverized material take-out section 18 arranged at the lower part of the pulverizers 2 and 3.
- An airtight seal 21 is provided between the peripheral edge of the crusher 3 and the gantry 13 to maintain an airtight state.
- a spacer 22 is provided between the lower part of the periphery of the crusher 3 and the gantry 13 so that the distance between the crushers 2 and 3 is kept constant.
- a jacket 23 is provided on the back surface of the pulverizer 3 so as to cool it through the refrigerant 24 inside.
- a supply path 26 for supplying the material 10 to be crushed from the hopper 25 communicates with the raw material supply unit 4, and a sensor 27 for detecting the presence or absence of the material 10 to be crushed is provided in the communication unit.
- the method for producing a pulverized product by using the above-mentioned apparatus includes forming a grinding part 5 and a pulverizing part 6 between a pair of opposing pulverizing surfaces of a pair of pulverizing machines 2 and 3, Rotate. Then, the raw material to be crushed 10 is supplied from the raw material supply unit 4 to the grinding unit 5 through the hopper 25 and the supply path 26, and the surface of the supplied pulverized material particles is ground by the grinding surfaces 2a and 3a and the material to be crushed. Coarsely grind the product particles.
- the ground and coarsely pulverized coarsely pulverized product is sheared, crushed and pulverized by the pulverizing unit 6, and the pulverized product 20 exiting from the pulverizing unit 6 is rotated in the annular passage 17 by rotating the grind piece 15 and the pulverizing machine 2, Crush it at the bottom of 3 and take it out from the pulverized material take-out part 18.
- FIG. 1 the gap between the lower side of the peripheral part of the crusher 2 and the gantry 13 is shown in a large figure. However, in practice, the gap is reduced and the fumes from the cooling gas jetting members 12a and 12b flow. Blockage by objects is prevented.
- the surface of the particles to be ground is ground by the grinding surfaces 2a and 3a by the rotation of the grinding machine 2, and the soft thin film such as the soft thin skin formed on the surface is destroyed, or While cracking, coarsely pulverize all or part of the particles to be crushed.
- the abrasive layer containing abrasive grains such as diamond particles as the grinding surface, the irregularly shaped granule particles protruding from the grinding surfaces 2a and 3a are easily pierced into the thin film and destroyed. All or a part of the particles to be crushed between 2a and 3a can be easily coarsely pulverized by the rotation of the pulverizer 2.
- the grinding surface 2a of the pulverizer 2 is formed with a receding grinding surface 2d, and the gap between the grinding surface 3a facing the receding grinding surface 2d is larger than that between the grinding surface 3a facing the reference grinding surface 2c.
- Coarse pulverization of large-diameter particles occurs in the part, and coarse pulverization of small-diameter particles occurs between the grinding surface 3a facing the reference grinding surface 2c. Since the deep groove 2e is formed on the reference grinding surface 2c as the material to be crushed, the large-diameter particles move toward the peripheral part of the reference grinding surface 2c from the reverse grinding surface 2d side, and partially rough.
- the deep groove 2e communicates with the reverse grinding surface 2d side at almost the same depth as the reverse grinding surface 2d, and the peripheral side is slightly closer to the front side of the reference grinding surface 2c and gradually becomes wider and deeper toward the tip side.
- the movement between the reference grinding surfaces 2c can be made uniform by making the deep grooves 2e radially and radially small. In this case, since the grinding object passage does not form a ground surface by abrasive particles or the like and is a smooth groove, it is possible to prevent the arcuate narrow groove 2f from being blocked.
- the coarsely pulverized material ground and coarsely pulverized in the grinding unit 5 is sheared, crushed and pulverized between the pulverizing surfaces 2b and 3b, and pulverized with a small particle size.
- Object 20 is formed.
- a soft thin film such as a thin skin that is broken or cracked in the grinding part 5 is also crushed to a small particle size by shearing and crushing between the grinding surfaces 2b and 3b, and the whole is uniform. It becomes a pulverized product with a small particle size.
- the crushing surfaces 2b and 3b have arc-shaped narrow grooves 2f and 3f extending radially from the center side to the peripheral side, the crushing effect by shearing and crushing is increased by the arc-shaped narrow grooves 2f and 3f, and crushing efficiency is increased.
- the arc-shaped narrow groove 2f is an arc-shaped narrow groove formed by laser processing, the edge portion is sharp and the grinding effect by shearing and crushing is great.
- the pulverizers 2 and 3 are cooled by the cooling unit, the pulverized material 10 and the pulverized material 20 can be cooled, thereby preventing deterioration in quality.
- the cooling unit the cooling unit provided adjacent to each of the crushers 2 and 3 is used, so that cooling suitable for each of the crushers 2 and 3 can be performed. That is, the rotary crusher 2 cools the crusher 2 by injecting the compressed gas generated by the compressed gas generator 14 from the cooling gas ejection members 12a and 12b into the cooling groove 11 and adiabatically expanding. The As a result, even in a rotary device, it is not necessary to tighten the seal as in the water-cooled type.
- the material to be crushed and the pulverized material in the part 6 can be cooled, and the introduction of the pulverized material into the annular passage 17 can be promoted.
- the fixed pulverizer 3 can be reduced to several tens with simple equipment and operation by passing the refrigerant 24 through the jacket 23 and sealing it with, for example, a water-cooled type. C can be cooled to a low temperature.
- FIG. 4 is a front view of the pulverizer 2 of the pulverized product producing apparatus of Example 2.
- the basic configuration of the grinding machine 2 of this example is the same as that of Example 1, except that the reverse grinding surface 2d of the grinding surface 2a is a diamond disc (diamond saw) 29 having a notch 28 in the peripheral portion. It is formed by mounting with mounting screws (not shown).
- the reference grinding surface 2c and other configurations are the same as in FIG.
- the manufacturing method of the pulverized material by the above apparatus is basically the same as that in FIG. 1, but when the diamond disk 29 on the reverse grinding surface 2d rotates with the rotation of the pulverizer 2, the particles to be pulverized The child is caught by the notch 28 and becomes easy to rotate, and the effect of breaking or cracking the thin film in the grinding part 5 is enhanced, and the grinding effect of the coarsely pulverized product in the grinding part 6 is increased.
- FIG. 5 is a front view of the pulverizer 2 of the pulverized material production apparatus of Example 3.
- the basic configuration of the grinding machine 2 of this example is the same as that of Example 2.
- the arc-shaped narrow groove 2f of the grinding surface 2b extends radially from the center side to the inner side of the peripheral end.
- the pulverized surface 2b is limited to a region from the center side to the inner side of the peripheral side end portion, and the rough surface processed portion 2g is formed in the peripheral side portion further than the pulverized surface 2b.
- the arcuate grooves 3f on the grinding surface 3b of the grinding machine 3 also radially extend from the center side force to the inner part from the peripheral edge, and the grinding surface 3b extends from the central side to the inner part from the peripheral edge.
- the rough surface processed portion 3g (not shown) is formed in a portion further on the peripheral side than the pulverized surface 3b.
- 30 is a mounting screw. Other configurations are the same as those in FIG.
- the method for producing a pulverized product using the above apparatus is basically the same as that shown in Figs. 1 and 2, but as the crushers 2 and 3 rotate, grinding of the peripheral parts of the pulverizers 2 and 3 is performed.
- the coarsely pulverized product ground and coarsely pulverized in Part 5 is sheared, crushed and pulverized between the pulverized surfaces 2b and 3b in the pulverized part 6, and the pulverized product with a small particle size is 2g, 3g on the peripheral side rough surface processed part. Further, it is further finely pulverized to form a powder frame 20 made of finely pulverized material.
- FIG. 6 is a longitudinal sectional view showing a pulverized material production apparatus of Example 4.
- the basic configuration of the pulverized material manufacturing apparatus 1 of this example is the same as that of Example 1.
- the pulverizers 2 and 3 are arranged in the horizontal direction, and the drive unit M and the gantry 13 are also in the horizontal direction.
- the ground material take-out section 18 and the hopper 25 are arranged in the same manner as in FIG. 1, and the raw material supply section 4 is integrated with the supply path 26.
- the method for producing a pulverized product using the above apparatus 1 is basically the same as that in FIG. 1, and the same effect as in FIG. 1 can be obtained.
- FIG. 7 shows the particle size distribution of the flour of hard wheat “Kitano Chiori” prepared using a diamond-coated mortar with the apparatus of FIG.
- the seed coat and the Aleurone layer were ground, resulting in a fine powder with a median diameter of 0.025 mm and an average grain size of 0.037 mm.
- a flour could be prepared.
- FIG. 8 shows the particle size distribution of hard wheat “Kitano Chiori” prepared using the same type of die without electrodeposition of diamond in the apparatus of FIG.
- the ground surface and the back ground surface cut by a lathe are smooth surfaces, so it is difficult to pulverize the seed coat and the Aleurone layer, and the mode diameter appears at a position of 0.128 mm.
- the 0.025mm peak in the endosperm part appears, so the particle size distribution consists of two peaks.
- the average particle size was 0.096 mm.
- the present invention can be applied to food materials such as wheat, rice, buckwheat, and soybean, and other pulverized materials, in particular, a method, an apparatus, and a pulverized material for pulverizing a granular material.
- the method can be applied to a method, an apparatus, and a pulverized product for producing a pulverized product having a uniform particle size by grinding and grinding the surface of the pulverized product particle by a pair of pulverizers arranged opposite to each other. .
- FIG. 1 is a longitudinal sectional view showing an apparatus for producing a pulverized product of Example 1.
- FIG. 2 is a front view of a crusher 2 of Example 1.
- FIG. 3 is a rear view of the crusher 2 of Example 1.
- FIG. 4 is a front view of a crusher 2 of Example 2.
- FIG. 5 is a front view of a crusher 2 of Example 3.
- FIG. 6 is a longitudinal sectional view showing an apparatus for producing a pulverized product of Example 4.
- FIG. 7 is a particle size distribution diagram of wheat flour by the pulverized product production apparatus of Example 2.
- FIG. 8 is a particle size distribution diagram of flour by the pulverized product production apparatus of Comparative Example 1. Explanation of symbols
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
Abstract
L’invention concerne un procédé d’élaboration d’un produit pulvérisé permettant, même en cas de pulvérisation de matières possédant une pellicule mince et souple, telles que des grains de céréales, de rompre efficacement la pellicule mince et souple pour pulvériser les matières grâce à un appareil et un processus simples et former ainsi un produit pulvérisé contenant de fines particules de taille uniforme. L’invention concerne également un appareil et un produit pulvérisé. Selon l’invention, une paire de planches de pulvérisation (2, 3) dont la partie centrale comporte des faces de mouture (2a, 3a) et dont la partie périphérique comporte des faces de pulvérisation (2b, 3b) sont disposées en regard l’une de l’autre pour former une partie de mouture (5) et une partie de pulvérisation (6) entre les faces opposées. Au moins une (2) des planches de pulvérisation est entraînée en rotation par un module d’entraînement (M), une matière (10) à pulvériser est introduite dans la partie de mouture à partir d’une partie d’alimentation en matière brute (4). La surface des grains de matière introduite est moulue dans la partie de mouture (5) et les grains sont soumis à un concassage grossier. Le produit grossièrement concassé est pulvérisé dans la partie de pulvérisation (6) et un produit pulvérisé (20) est évacué d’une partie d’évacuation (18) située dans la partie de pulvérisation.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005106903A JP4806829B2 (ja) | 2005-04-01 | 2005-04-01 | 粉砕物の製造方法および装置 |
| JP2005-106903 | 2005-04-01 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2006109422A1 true WO2006109422A1 (fr) | 2006-10-19 |
Family
ID=37086713
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2006/305397 Ceased WO2006109422A1 (fr) | 2005-04-01 | 2006-03-17 | Procede d’elaboration d’un produit pulverise, appareil et produit pulverise |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP4806829B2 (fr) |
| WO (1) | WO2006109422A1 (fr) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012217955A (ja) * | 2011-04-12 | 2012-11-12 | Terada Seisakusho Co Ltd | 粉砕機 |
| WO2018168184A1 (fr) * | 2017-03-17 | 2018-09-20 | 日本コークス工業株式会社 | Pulvérisateur |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6296431B2 (ja) * | 2012-05-28 | 2018-03-20 | ナチュラルプロセスファクトリー株式会社 | クッキー用の食品の加工方法 |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58193742A (ja) * | 1982-05-07 | 1983-11-11 | 増幸産業株式会社 | 摩砕装置 |
| JPS60106547A (ja) * | 1983-11-14 | 1985-06-12 | 旭松食品株式会社 | 磨砕成形機 |
| JPS62106850A (ja) * | 1985-10-31 | 1987-05-18 | 京セラ株式会社 | 磨砕装置 |
| JPH031061B2 (fr) * | 1986-10-02 | 1991-01-09 | Tsuneo Masuda |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61167947U (fr) * | 1985-04-08 | 1986-10-18 | ||
| JPH0451874Y2 (fr) * | 1988-03-18 | 1992-12-07 | ||
| JP2949290B2 (ja) * | 1989-07-26 | 1999-09-13 | 京セラ株式会社 | アモルファスシリコン系半導体膜の製法 |
| JP2003048086A (ja) * | 2001-07-31 | 2003-02-18 | Canon Inc | エネルギービーム加工装置及び加工方法 |
-
2005
- 2005-04-01 JP JP2005106903A patent/JP4806829B2/ja not_active Expired - Fee Related
-
2006
- 2006-03-17 WO PCT/JP2006/305397 patent/WO2006109422A1/fr not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58193742A (ja) * | 1982-05-07 | 1983-11-11 | 増幸産業株式会社 | 摩砕装置 |
| JPS60106547A (ja) * | 1983-11-14 | 1985-06-12 | 旭松食品株式会社 | 磨砕成形機 |
| JPS62106850A (ja) * | 1985-10-31 | 1987-05-18 | 京セラ株式会社 | 磨砕装置 |
| JPH031061B2 (fr) * | 1986-10-02 | 1991-01-09 | Tsuneo Masuda |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012217955A (ja) * | 2011-04-12 | 2012-11-12 | Terada Seisakusho Co Ltd | 粉砕機 |
| WO2018168184A1 (fr) * | 2017-03-17 | 2018-09-20 | 日本コークス工業株式会社 | Pulvérisateur |
| JP2018153757A (ja) * | 2017-03-17 | 2018-10-04 | 日本コークス工業株式会社 | 粉砕機 |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4806829B2 (ja) | 2011-11-02 |
| JP2006281140A (ja) | 2006-10-19 |
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