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WO2004091761A1 - Procede permettant de melanger une matiere premiere en poudre et une matiere premiere liquide - Google Patents

Procede permettant de melanger une matiere premiere en poudre et une matiere premiere liquide Download PDF

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Publication number
WO2004091761A1
WO2004091761A1 PCT/JP2003/008119 JP0308119W WO2004091761A1 WO 2004091761 A1 WO2004091761 A1 WO 2004091761A1 JP 0308119 W JP0308119 W JP 0308119W WO 2004091761 A1 WO2004091761 A1 WO 2004091761A1
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WO
WIPO (PCT)
Prior art keywords
blade
cylinder
wall
liquid
powder material
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
Application number
PCT/JP2003/008119
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English (en)
Japanese (ja)
Inventor
Naganobu Hayabusa
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Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to AU2003304039A priority Critical patent/AU2003304039A1/en
Publication of WO2004091761A1 publication Critical patent/WO2004091761A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • A—HUMAN NECESSITIES
    • A21—BAKING; EDIBLE DOUGHS
    • A21D—TREATMENT OF FLOUR OR DOUGH FOR BAKING, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS
    • A21D8/00—Methods for preparing or baking dough
    • A21D8/02—Methods for preparing dough; Treating dough prior to baking
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/62—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis comprising liquid feeding, e.g. spraying means
    • B01F27/621—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis comprising liquid feeding, e.g. spraying means the liquid being fed through the shaft of the stirrer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/70—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms
    • B01F27/707—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms the paddles co-operating, e.g. intermeshing, with elements on the receptacle wall

Definitions

  • the present invention relates to a technique for combining a powder material and a liquid material.
  • Particulate power S Fine like flour that contains a lot of air between the particles f This raw material can not easily eliminate bonding unevenness once it causes bonding unevenness.
  • fine particles »As fine unit air has the property of adhering to powder particles, it is because air gives way to the liquid source to be diffused. Then, it takes a long time to spread, and it takes stirring and mixing for the powdery raw material which has the property that the previously produced darten yarn and weave is destroyed by the force of agitation such as wheat flour. It can only be done until some time. It is the limit of agitation mixing at which the amount of newly produced darten weave by agitation mixing is balanced with the amount of destruction of the previously produced darten weave.
  • the amount of gluten yarn that is destroyed from the amount of gluten weave produced is greater: the amount of E-woven increases, and the gluten fiber that can be obtained by continuing stirring and mixing decreases. Therefore, it is necessary to break up the confection before the amount of goreten yarn _ ⁇
  • Flow Jetta I for the addition of flour is a stock meeting: fc 3 ⁇ 4 and is a modified version of Roh's humidifier / J / for adding water to wheat flour, and the material dropped is micronized and blown tangentially It is a device in which the speed of the acting disk is increased by ISi, and a large number of pins for stirring are modified at the periphery of the disk. It is a useful apparatus for continuous addition of water to wheat flour.
  • liquid raw material such as salt water drops in a cylindrical shape on the disk, so the device is installed horizontally and the liquid raw material will be evenly ejected in the entire circumferential direction. Because flour is simply dropped around the center of the disc, it does not fall evenly around the center, and there is a large difference in the amount of flour that is blown depending on the direction. Because of this, flour and liquid ingredients such as t ⁇ are drained out of even bonds.
  • This system in which powder material and liquid material are simultaneously dropped onto the disc to make fine particles, can not be used in patch-type mixers.
  • this type of equipment is difficult to supply both raw materials at a ratio such as when starting supply of powder raw materials and liquid raw materials and when stopping supply, it is suitable for processing small amounts of raw materials. Kana Re.
  • This tb reservoir is used as a patch-type mixer in which the powder material forms a layer, even if the direction of the blades, the powder material inlet, the number of nozzles, and the combination material outlet are renewed. It is not possible.
  • this type of device has a small amount of raw material because it is difficult to supply both raw materials at the same ratio as when starting supply of powder raw materials and liquid raw materials and when stopping supply. It is not suitable for
  • the super turbo for flour addition is basically the same device as the turbulizer for flour addition. While the rotating blades of the turbulizer are paddle-like, the rotating blades of the super turbo are plate-like and round-bar-like. There is a problem similar to that of the turbulizer, and for the same reason as the turabilizer, it can not be used for patch type equipment and it is not suitable for small amount of raw material processing.
  • a Japanese-made flour that improves the convenience for cleaning by improving the power of the rotary buraiza or super turbo type mixer, supporting the rotary shaft with only the raw material supply end and driving it, and removing the cylinder easily from the discharge end.
  • the entire system is miniaturized and easy to clean, making it a useful mixer.
  • the Turbulizer and Super Turbo the problems with Karo water matter are the same. Therefore, it is recommended to perform agitation processing with a vacuum mixer in order to equalize water after adding water with this mixer. It is done. It is no different from conventional Turbulizers and Super Turbos in that it is a modification that can not be applied to patch types.
  • a mixer called a vacuum mixer has been supplied for some time. It is a mixer that performs stirring and mixing while degassing the inside of the container. Since the liquid raw materials are efficiently diffused and penetrated into the powder raw materials by eliminating the interference of air contained in the powder raw materials, gluten is well organized if it is used for carolizing water to the flour quickly. However, the food produced using this mixer lacks the taste and flavor as a food. In the process of mixing, the air power S in the raw material is eliminated, the air is reduced, the air contains less force, and it becomes a food, so the stimulation of the taste component to the miso becomes continuous when it is roasted, and the nature of human miso Because it is difficult to feel the taste and taste of food. It is inevitable that mixers that perform degassing and stirring and mixing have major drawbacks as mixers for food production.
  • Patent application publication 6 3 2 5 5 5 2 7 is a mixing technology for adding a liquid material from a rotating blade. If a spout is provided at the tip of the blade and water is injected, water will be injected into the powder material at the tip of the blade. Therefore, it can not be avoided that the liquid raw material is excessively added to the powder raw material. The applicant also says that if a jet is provided at a position opposite to the rotational direction of the blade to eject water, the pressure is negative because the rear portion of the blade has a negative pressure, resulting in water mist. Certainly, vortices and turbulence occur in the rear of the blade and negative pressure is generated.
  • the property that the water droplets try to be water droplets is strong, and it can not be hydrophobized into fine particles under negative pressure due to the swirling and turbulent flows of the stirring blades.
  • the water ejected from the rear of the blade may not become fine even if it may become a small water droplet.
  • Small water droplets are made of flour composed of fine particles It is a huge body of water. Whether the unit is large or small, once the excess water is added to the wheat flour, this is mixed and mixed to challenge difficult water diffusion. Re, unlike the type mixer.
  • Patent application publication No. 5 7 1 3 6 9 2 5 5 says that the water jet provided on the rotating shaft rotates so that the water S is micronized like a spring apparatus.
  • the device is a device that prevents the water from being scattered and scattered. If the equipment's hydroparticulated S is used, the amount of evaporating water increases and the springing effect is intensified.
  • Liquids that tend to bond with each other like water are such techniques that allow the liquid to become dispersed by subjecting ⁇ liquid to maintain its bond to a large acceleration and tearing it apart » It is impossible to achieve micronization without means based on the above. Therefore, the present invention solves the following.
  • the powdery raw material containing a large amount of fine unit air between the particles because of the fineness of the particle power S forms a portion which is once excessively connected to the liquid raw material. Because air prevents the liquid material from diffusing and permeating the powder material, it becomes difficult to spread the liquid material evenly to the powder material, and uniform bonding can not be easily achieved. . It takes a long time to reach a practical range of uniform blanches, and if the generated gluten paper weave is to be added to the flour to be destroyed by stirring and mixing, the water is spread throughout the wheat flour. You will have to release the purpose itself early.
  • the liquid raw material inside which contains a large amount of air between the particles, such as wheat flour, which has a fine particle power S, which makes it easy to make the powder raw material fine as water.
  • Add liquid ingredients When combining both raw materials do not make excess bonds. ⁇
  • the method can be used for continuous mixing, patch type mixing, mixing of a large amount of raw materials, and mixing of a small amount of raw materials. Disclosure of the invention
  • the powder material is rotated along the cylinder or the inner wall of the container conforming to the cylinder. At this time, it is made to prevent the occurrence of excessive acceleration which impedes the intra-cylindrical plasticity of the combination of the powder raw material and the liquid raw material and the non-bond inside the layer of powder raw material.
  • the fine particle-like liquid material is added to the powder material from the side of the rotating shaft.
  • the powder raw material forms a layer
  • the combined substance which increases the mass by bonding with the particulate liquid raw material in the surface layer on the rotary shaft side of the layer moves to the side of the inner wall of the layer as it rotates. Do. Instead, in the surface layer on the rotating shaft side, the liquid material and the non-bonded material appear small, and the powder material appears. It is the principle of a cyclone. If bonding progresses and the whole becomes a bond, the degree of bonding is small! / ⁇ A relatively small mass of binding material appears on the surface layer on the rotating shaft side and combines with the particulate liquid material. At this stage, reduce the amount of fine particle liquid feed per unit time.
  • the tip In order to rotate the powder material along the inner wall of the cylinder, the tip reaches the powder material rotating along the inner wall, and a rotary blade is provided to act on the powder material, and the powder material is rotated along the inner wall.
  • the blade can be rotated by an acceleration that prevents pressure on the inner wall from causing excessive pressing of the powder material.
  • blades or protrusions acting on the powder material may be provided on the inner wall of the cylinder, and the powder material may be rotated along the inner wall by the blades or protrusions, and the pressure on the inner wall of the cylinder may be excessive.
  • the cylinder is rotated at a speed at which acceleration occurs.
  • the front end In order to atomize the liquid raw material into the powder raw material rotating along the inner wall of the cylinder and add it from the side of the rotating shaft, it is possible for the front end to reach the powder raw material rotating along the inner wall. For example, set the blade on the rotary shaft. If the tip of the blade is not in contact with the powder material, the liquid source to be supplied at a supply amount that will not cause bonding in the surface layer to exceed the final bonding rate, the tip of the blade, blade tip The department contacts powder material! If it is shaken, it will be emitted from the side edge and made into fine particles.
  • a blade at the tip of the blade rotates the blade at a rate that results in an acceleration that can atomize the liquid source supplied to the side edge under the amount supplied.
  • the blades and rods acting on the powder material may be integrated with the blades acting on the liquid material, the blades and rods acting on the powder material may be separated separately, and the blades acting on the liquid material may be separated.
  • the blades can also be rotated separately to produce the optimum acceleration for each. As will be described later, how to drive both blades in a row S Functionally the most preferred level.
  • FIG. 1 is a view showing the principle of an apparatus in which a long blade for rotating a powder material along the inner wall of a cylinder and a short blade for atomizing a liquid material and releasing it on the same rotation axis.
  • the inlet for powder material provided on the cylinder and the outlet for combined substances were omitted. Variations in the direction of the blades that move the powder material in the left and right directions were also omitted.
  • the holes for supplying liquid material to the lower front of the blade are drawn larger than the actual ratio.
  • FIG. 2 is a cross-sectional view of the plane including the line connecting ab in FIG. 1, which is rotated 90 ° from that in FIG.
  • the dotted line shows the blade at a position away from the plane connecting the a b.
  • the arrows at the top of the cylinder indicate the direction of rotation of the long and short blades.
  • FIG. 3 is a view showing the principle of an apparatus for separately driving a blade for rotating a powder material along the inner wall of a cylinder and a blade for finely discharging a liquid material and discharging the material.
  • a blade for rotating the powder material along the inner wall of the cylinder is provided at a position opposite to the rotary shaft, and a horizontally long blade for atomizing the liquid material and releasing it, a passage for the liquid material, namely a feed pipe
  • This is a device with two pieces in total: one on the opposite side of the thick rotary shaft across the rotary shaft.
  • FIG. 10 is a cross-sectional view of a plane including the blades and the rotation axis in a state in which all the blades of this device are stopped so as to be located on the same plane.
  • the liquid material is supplied to the inside of the large diameter rotary shaft, that is, from the supply pipe through the small hole to the lower front of the blade. This is an example of the embodiment described on the ninth line on page 18.
  • the blades acting on the powder material are attached to a curved plate along the inner wall surface of the cylinder connecting the two flanges.
  • the inlet for powder material provided on the cylinder and the outlet for combined substances were omitted.
  • the change in the direction of the blade that moves the powder basics in the left or right direction was also omitted.
  • Liquid material in the lower front of the blade The holes supplied are drawn larger than the actual ratio.
  • FIG. 4 is a cross-sectional view of the plane including the line connecting ab in FIG. 3, with FIG. 3 being rotated 90 °.
  • Point # The fountain shows a blade located away from the plane connecting a b.
  • the arrows at the top of the cylinder indicate the direction of rotation of the blades acting on the powder material and the blades acting on the liquid material.
  • FIG. 5 shows the principle of a cylinder for rotating the powder material along the inner wall of the cylinder and an apparatus for driving the blade for atomizing the liquid material and discharging it.
  • FIG. 10 is a cross-sectional view of a plane including the blades and the rotation axis in a state in which all the blades of this device are stopped so as to be located on the same plane.
  • the liquid material is supplied to the inside of the large diameter rotary shaft, that is, from the supply pipe through the small hole to the lower front of the blade. This is an example of an embodiment described on the ninth line on page 19.
  • the inlet for powder material provided on the cylinder and the outlet for combined substances were omitted. Variations in the direction of the blades that move the powder material in the left and right directions were also omitted.
  • the holes for supplying liquid material to the lower front of the blade are drawn larger than the actual ratio.
  • FIG. 6 is a cross-sectional view of the plane including the line connecting ab in FIG. 5, with FIG. 5 being rotated 90 °.
  • the dotted line shows the blade at a position away from the plane connecting the a b.
  • the arrows at the top of the cylinder indicate the direction of rotation of the blades acting on the powder material, the cylinder and the blades acting on the liquid material.
  • FIG. 7 is a cross-sectional view of a plane including a blade having an inner diameter of the liquid material passage and blades of a device provided with a plurality of blades at positions opposed to each other across the rotation axis on the rotation axis.
  • the liquid material is supplied to the inside of the thick rotary shaft, that is, from the supply pipe through the small hole to the lower front of the blade. This is an example of the embodiment to be described on the 14th line of the 19th page.
  • the inlet for powder material provided on the cylinder and the outlet for combined substances were omitted. Variations in the direction of the blades that move the powder material in the left and right directions were also omitted.
  • the holes for supplying liquid material to the lower front of the blade are drawn larger than the actual ratio! /.
  • FIG. 8 is a cross-sectional view of the plane including the line connecting ab in FIG. 7, with FIG. 7 being rotated 90 °.
  • the dotted line shows the part of the blade located away from the plane connecting the a b.
  • the arrow at the top of the cylinder indicates the direction of rotation of the blades.
  • FIG. 9 is a view showing the principle of an apparatus in which a blade is provided on a rotary shaft which has a tip for rotating a powder material along the inner wall of a cylinder, and which discharges the liquid material from the opposite side end. It is.
  • the liquid source is supplied to the inside of the thick rotary shaft, that is, from the supply pipe through the small hole to the lower front of the side end of the inverted V of the blade.
  • the inlet for powder material provided on the cylinder and the outlet for combined substances were omitted. Variations in the direction of the blades that move the powder material in the left and right directions were also omitted.
  • the holes for supplying liquid material to the lower front of the blade are drawn larger than the actual ratio.
  • FIG. 10 is a cross-section of the plane including the line connecting the abs of FIG. 9 and 90 ° rotated from that of FIG. FIG.
  • the dotted line shows the blade and the portion of the blade located away from the plane connecting ab.
  • the arrow at the top of the cylinder indicates the direction of rotation of the blades.
  • FIG. 1 1 shows that it has a rod-shaped tip that rotates the powder material along the inner wall of the cylinder, so that it does not reach the powder material, it has a second tip at a low position, low position, low position.
  • FIG. 16 is a diagram showing the principle of an apparatus in which a multistage vane for finely atomizing and discharging a liquid raw material from the front view is provided on a rotating shaft.
  • FIG. 6 is a cross-sectional view of a plane including a blade of an apparatus in which multi-stage type vanes are arranged at opposing positions with a thick plate whose inside is used as a passage of liquid material and a rotary shaft.
  • the liquid material is supplied to the inside of the thick rotary shaft, that is, from the supply pipe through the small hole to the lower front of the second tip of the blade. This is an example of the embodiment to be described on the 2nd line of page 20.
  • the inlet for powder material provided on the cylinder and the outlet for combined substances were omitted. Variations in the direction of the blades that move the powder material in the left and right directions were also omitted.
  • the holes for supplying liquid material to the lower front of the blade are drawn larger than the actual ratio.
  • Fig. 12 is the surface including the line connecting ab in Fig. 11 with 90 in Fig. 11. It is a cross-sectional view with the direction changed. The dotted line shows the blade at a position away from the plane connecting the a b.
  • a large diameter rotary shaft attached with a rotating blade acting on the powder material and a rotating blade for atomizing the liquid material, the inside of which constitutes a supply tube for the liquid material
  • a long blade for rotating the powder material along the inner wall and a short blade for atomizing the liquid material are provided on the same rotating shaft,
  • the latter is a form in which the liquid raw material micronized is added to the powder raw material rotating along the inner wall from the side of the rotation shaft.
  • the blade acting on the powder material and the blade acting on the liquid material are provided on the same rotary shaft.
  • An acceleration occurs. If the action of the blade '3 or the like, which rotates the powder material along the inner wall, is too strong, the powder material is strongly pressed against the inner wall, and the combined product of the liquid material and the mass increase the strength of the inner wall of the layer. As it moves, instead, the unbound powder material appears on the side of the rotating shaft, and the movement of bound and unbound materials inside the layer is impeded.
  • the method of supplying the liquid material is not limited to the method shown in this figure, but a method of supplying the liquid material to the front of the blade from a conduit provided on the rotating shaft, guiding the liquid material through the blade to the tip, There are various ways to make the inside of the blade function in the same way as the front of the blade in this figure, etc.
  • the blade acting on the powder material and the blade acting on the liquid material can be alternately provided in a large number at various angles over the width of the rotation shaft.
  • the liquid raw material can be added in the first half, and the structure can be made in the second half with kneading.
  • the powder raw material is put into the container, and the blades are rotated to wait for the powder raw material to form a layer rotating along the inner wall of the cylinder, and the liquid raw material is micronized. It waits for the acceleration which can make the liquid material particulate in the tip part, and starts the supply of the liquid material. If the patch type device is used to add water to flour etc., reduce the speed of the blades immediately after the completion of the addition and start kneading.
  • the cylinder and container may be horizontal or bowl-shaped.
  • the axis of rotation is horizontal, and the axis of rotation is also vertical when.
  • the blades for rotating the powder material along the inner wall and the blades for atomizing the liquid material are provided on the rotating shaft separately. Rotate each blade at a speed that is most suitable for the function of each blade, and rotate the liquid material that has been atomized into a ii state into a powder material that rotates at an optimal speed along the inner wall. It is a form added from the side of the axis. It is a form which can implement this invention most effectively.
  • a flange 18 is provided on the rotary shaft 17 along both ends of the inside of the cylinder, and a curve which rotates along the inner wall between the two flanges Pass the nineteenth board.
  • the curved plate is provided with blades 13 acting on the powder material. The powder material can be rotated along the inner wall of the cylinder 11, and the blade 13 etc. is rotated at such a speed that the caro speed is generated in the blade 13 etc.
  • the tip of the blade does not reach the powder material that rotates along the inner wall! / Rotor blade 14 A rotation shaft that drives separately from the rotation shaft 17
  • the blades 14 and so on are rotated at a speed that produces a caro speed at which the liquid raw material can be finely divided and placed at the tip thereof.
  • a long reed along the rotation axis, and a series of blades provided with a total of two ones each across the rotation axis, but even if it is not a long blade, You don't have to be two blades.
  • the blade 14 for atomizing the liquid raw material can be rotated at a sufficiently high speed as needed, the liquid raw material can be atomized, and the liquid raw material per unit time.
  • the amount supplied can also be adjusted to the optimum condition as needed.
  • FIGS. 5 and 6 are basically the same as the devices of FIGS. 3 and 4.
  • the apparatus shown in FIGS. 3 and 4 uses a blade acting on the powder material provided from the rotation shaft via the flange and the curved plate.
  • the cylinder 21 itself is rotated to provide the inner wall of the cylinder with a blade acting on the powder material or a projection instead of the blade.
  • the liquid material to be supplied to the root of the front surface of the blade is powder raw material by centrifugal force. Move toward the tip of the V-shaped blade, and is added to the powder material without being finely divided. Therefore, in order to guide the liquid material moving on the front of the blade to one side and emit it from the side plate 34 into fine particles, the side end is raised so as to form an acute angle with the direction of the length of the rotation shaft. However, only the side end on the inner wall side has only to form an acute angle with the direction of the length of the rotation axis since the liquid source is released at the side end on the inner wall side of the cylinder.
  • the method of leading the liquid material to the side end near the edge of the front of the blade for example, the direction of the blade is directed diagonally to the direction of rotation, etc.
  • the method of providing the side end on the inner wall side so as to form an acute angle with the direction of the length of the rotating shaft as shown in FIGS. 7 and 8 is one of the methods of reliably guiding the liquid material to the side end.
  • an acceleration for rotating the powder material along the inner wall is generated at the tip of the blade provided on the rotating shaft, and the force is applied to the side of the same blade.
  • a guide is provided on the front of the blade to guide the liquid material to be supplied to the root of the front of the blade to one side or both sides of the blade, and so on.
  • the liquid material supplied to the root of the front of the blade is led to the side edge of the inverted V shape.
  • the liquid material can also be led directly to the side end through a conduit provided in or on the surface of the blade.
  • the equipment whose principle diagram is shown in Figures 1 1 and 12
  • the caro speed that is rotated along the inner wall is generated, so that the powder material of the inner wall of the cylinder can be delivered to the powder material of the cylinder near the rotation axis of the blade.
  • an accelerating velocity is generated, and the atomized liquid material is added to the powder material rotating along the inner wall of the cylinder from the side of the rotating shaft.
  • the liquid material may come into contact with the powder material. make it a simple structure.
  • the liquid material supplied to the root of the front of the blade comes in contact with the powder material and is led to the reed, tip, and 33 ⁇ 43 ⁇ 4.
  • the mixing time required to equalize the water content was reduced to 30 seconds or less when the dough for baking was subjected to watering at 60 ° / 0 or more, which has taken 5 minutes or more.
  • the blade functioning as the powder material of the present invention and the blade functioning as the liquid material are separately driven. Using the mechanism to change the degree of atomization of the liquid raw material according to the situation of the powder raw material and to change the supply amount of the liquid raw material per By combining the powdery material with the liquid material, it becomes possible to easily realize uniformly bonding a small amount of the liquid material to the fine powder material, which has been difficult until now.
  • the method of the present invention is used, the method of assembling different bonding methods depending on the nature of the raw material to be bonded is assembled, and the method of assembling the most bonding is assembled to create the desired property of the bonding material. It became possible to combine
  • the liquid raw material can be added to the powder raw material under weightlessness, even with high efficiency and maintaining high efficiency. Industrial applicability
  • Powder raw material power Fine particles in the form of fine particles containing gas between the particles, so mixing of liquid raw material is not easy mixing of powder raw material and liquid raw material is carried out in the industrial wide-spreading field. The effect of the improvement is dramatically large, and the form is simple and practical. S Easy This technology has high industrial applicability.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

La présente invention concerne un procédé efficace qui permet d'ajouter de l'eau à un mélange de matière première en poudre constituée de particules et de matière première liquide. Selon les procédés classiques, on mélange d'abord les deux matières premières afin de produire une liaison de matière non uniforme, et l'on agite ensuite le mélange afin d'obtenir une liaison uniforme. On peut augmenter l'efficacité des procédés classiques en ajoutant, depuis un côté d'axe de rotation, une matière première liquide particulaire à une matière première en poudre que l'on fait tourner le long de la paroi interne d'un cylindre creux. La matière première en poudre tourne le long de la paroi interne du cylindre creux sous l'effet d'une accélération produite par des lames de rotation qui atteignent la matière première en poudre tournant le long de la paroi interne du cylindre creux. L'axe de rotation produit une accélération sur les parties bouts ou sur les parties extrémités latérales des lames qui n'atteignent pas la matière première en poudre. L'accélération permet de transformer en particules la matière première liquide relâchée par les parties bouts ou extrémités latérales. La matière première liquide transformée en particules est ajoutée, depuis le côté axe de rotation, à la matière première en poudre tournant le long de la paroi interne du cylindre creux. Un objet lié dont la masse est augmentée par la liaison entre la matière première liquide et une couche, coté axe de rotation, de matière première en poudre tournant le long de la paroi interne du cylindre creux se déplace sur le côté de la paroi interne. Une partie non liée de petite masse de matière première en poudre apparaît dans la couche superficielle de la matière première en poudre du côté axe de rotation, qui est efficacement liée à la matière première liquide particulaire.
PCT/JP2003/008119 2003-04-16 2003-06-26 Procede permettant de melanger une matiere premiere en poudre et une matiere premiere liquide Ceased WO2004091761A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2003304039A AU2003304039A1 (en) 2003-04-16 2003-06-26 Method of mixing powder raw material and liquid raw material.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2003145534 2003-04-16
JP2003-145534 2003-04-16

Publications (1)

Publication Number Publication Date
WO2004091761A1 true WO2004091761A1 (fr) 2004-10-28

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PCT/JP2003/008119 Ceased WO2004091761A1 (fr) 2003-04-16 2003-06-26 Procede permettant de melanger une matiere premiere en poudre et une matiere premiere liquide

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103109884A (zh) * 2012-12-02 2013-05-22 乐正午 一种转动管式和面装置
CN105854708A (zh) * 2016-06-06 2016-08-17 无锡市翱宇特新科技发展有限公司 一种高效化工原料混合装置
CN106320150A (zh) * 2016-10-21 2017-01-11 西安建筑科技大学 一种钢渣沥青透水混合料双轴双拌合装置及拌合工艺
CN106512826A (zh) * 2016-12-04 2017-03-22 重庆市江津区驴溪酒厂有限责任公司 制酒用搅拌装置
GB2569941A (en) * 2017-11-17 2019-07-10 Xaar 3D Ltd Apparatus for the manufacture of three-dimensional objects
CN111010970A (zh) * 2019-12-31 2020-04-17 重庆酷熊科技有限公司 一种用于液态有机肥的施肥装置
CN111034446A (zh) * 2019-12-31 2020-04-21 重庆酷熊科技有限公司 一种腐殖酸有机肥施肥设备

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JPS57136925A (en) * 1981-02-18 1982-08-24 Hoshino Bussan Kk Continuous and homogeneous hydromixer
JPS58141726U (ja) * 1982-03-19 1983-09-24 株式会社新明製作所 固形飼料用糖蜜ミキサ−装置
JPS63214328A (ja) * 1987-09-25 1988-09-07 Kitagawa Tekkosho:Kk 横多軸型混合装置
JPS63251059A (ja) * 1987-04-06 1988-10-18 Tooc Kogyo Kk パスタの製造方法および製造装置
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JP2001079827A (ja) * 1999-09-10 2001-03-27 B M Syst:Kk 管路内混合装置

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JPS5640425A (en) * 1979-09-08 1981-04-16 Yasuro Ito Continuous mixing method and apparatus therefor
JPS55119430A (en) * 1980-02-15 1980-09-13 Nisshin Flour Milling Co Ltd Mixing device of powder and granular material
JPS57136925A (en) * 1981-02-18 1982-08-24 Hoshino Bussan Kk Continuous and homogeneous hydromixer
JPS58141726U (ja) * 1982-03-19 1983-09-24 株式会社新明製作所 固形飼料用糖蜜ミキサ−装置
JPS63251059A (ja) * 1987-04-06 1988-10-18 Tooc Kogyo Kk パスタの製造方法および製造装置
JPS63214328A (ja) * 1987-09-25 1988-09-07 Kitagawa Tekkosho:Kk 横多軸型混合装置
US5372424A (en) * 1992-03-18 1994-12-13 Assistance Maintenance Industrielle Gildasienne Screw mixer, particulary for foundry molds
JP2001079827A (ja) * 1999-09-10 2001-03-27 B M Syst:Kk 管路内混合装置

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103109884A (zh) * 2012-12-02 2013-05-22 乐正午 一种转动管式和面装置
CN105854708A (zh) * 2016-06-06 2016-08-17 无锡市翱宇特新科技发展有限公司 一种高效化工原料混合装置
CN106320150A (zh) * 2016-10-21 2017-01-11 西安建筑科技大学 一种钢渣沥青透水混合料双轴双拌合装置及拌合工艺
CN106512826A (zh) * 2016-12-04 2017-03-22 重庆市江津区驴溪酒厂有限责任公司 制酒用搅拌装置
GB2569941A (en) * 2017-11-17 2019-07-10 Xaar 3D Ltd Apparatus for the manufacture of three-dimensional objects
CN111010970A (zh) * 2019-12-31 2020-04-17 重庆酷熊科技有限公司 一种用于液态有机肥的施肥装置
CN111034446A (zh) * 2019-12-31 2020-04-21 重庆酷熊科技有限公司 一种腐殖酸有机肥施肥设备
CN111010970B (zh) * 2019-12-31 2021-01-29 重庆酷熊科技有限公司 一种用于液态有机肥的施肥装置

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