WO2004091761A1 - Method of mixing powder raw material and liquid raw material. - Google Patents

Method of mixing powder raw material and liquid raw material. Download PDF

Info

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
Authority
WO
WIPO (PCT)
Prior art keywords
blade
cylinder
wall
liquid
powder material
Prior art date
Application number
PCT/JP2003/008119
Other languages
French (fr)
Japanese (ja)
Inventor
Naganobu Hayabusa
Original Assignee
Naganobu Hayabusa
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 Naganobu Hayabusa filed Critical Naganobu Hayabusa
Priority to AU2003304039A priority Critical patent/AU2003304039A1/en
Publication of WO2004091761A1 publication Critical patent/WO2004091761A1/en

Links

Classifications

    • AHUMAN NECESSITIES
    • A21BAKING; EDIBLE DOUGHS
    • A21DTREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
    • A21D8/00Methods for preparing or baking dough
    • A21D8/02Methods for preparing dough; Treating dough prior to baking
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/62Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis comprising liquid feeding, e.g. spraying means
    • B01F27/621Mixers 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/70Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms
    • B01F27/707Mixers 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.

Abstract

An efficient method of adding water to a mixture of a powder raw material formed from particles and a liquid raw material. In a conventional technique, both materials are first mixed to produce un-uniform material bonding, and then the mixture is agitated for uniform bonding. Such inefficiency is eliminated by adding a particulate liquid raw material from the side of a rotation shaft to a powder raw material that is rotated along the inner wall of a hollow cylinder. Powder raw material is rotated along the inner wall of a hollow cylinder by acceleration produced at rotation blades that reach the powder raw material rotating along the hollow- cylinder inner wall. The rotation shaft produces acceleration at the tip portions or side end portions of blades that do not to reach the powder raw material. The acceleration causes the liquid raw material that is released from the tip portions or side end portions to be turned into particles. The liquid raw material turned into particles is added from the rotation shaft side to the powder raw material rotating along the hollow-cylinder inner wall. A bonded object whose mass was increased by the bonding of the liquid raw material with a rotation shaft-side layer of the powder raw material along the hollow-cylinder inner wall moves to the inner wall side. An un-bonded portion with small mass of the powder raw material appears in the surface layer of the powder material on the rotation shaft side and is efficiently bonded to the particulate liquid raw material.

Description

明 細 書 粉体原料と液体原料のミキシング方法 技術分野  Method of mixing powder material and liquid material
この発明は、 粉体原料と液体原料を結合させるミ '技術に関するものである 技 景  The present invention relates to a technique for combining a powder material and a liquid material.
小麦粉に をカロえて製麵用の生地をつくる際の攪拌混合は、 粉体原料に液体原料 を結合させる従来技術の典型的な一例である。 さまざまな形状の攪拌羽根や攪拌棒を持 つ攪拌混合型のミキサ一が使用されてきた。 しかし、 « ^の生地つくりのように小 麦粉に対して重量比 3 0 %から 4 0数%の加水をおこなうにも、 また手加 麵の生地 つくりのように 4 0数%から 5 0 %の加水をおこなうにも、 2 0分に近レ、時間を要する。 しかも、 2 0分に近い攪拌混合によって: ¾7_Κを小麦 立子の全てにゆきわたらせること ができるわけではなレヽ。 粒子力 S微細でその粒子の間に多量の空気を含む小麦粉のような 粉 f本原料の 、 一旦結合むらを生じさせると結合むらを容易に解消することができな V、。微細な粒子の間に雜する »細な単位の空気は粉体粒子に付着する性質を示すため、 拡散しょうとする液体原料に空気が道を譲らなレ、ためである。 すると拡散に長レ、時間を 要するだけでなく、 小麦粉のように先に生成されたダルテン糸且織が攪掛昆合の力で破壊 される性質を持つ粉体原料の には、 攪拌混合をある までしかおこなうことがで きない。 攪拌混合によって新たに生成されるダルテン紙織の量と、 それまでに生成され たダルテン紙織が破壊される量がバランスする時点カ攪拌混合の限界である。 それ以上 に攪拌混合を続けると生成されるグルテン紙織の量より破壊されるグルテン糸: E織の量が 多くなり、 攪拌混合を続けることによつて得ることができるグルテン繊は減少する。 従って破壊されるグノレテン糸_§|哉の量が多くなる前に攪 昆合を打切るのであるが、 生地 の中には、 過剰に加水された部分や未加水の部 グルテンの繊が破壊された部分が 多ぐ雜し、 これが加水率が 5 0 %以下でも生地ゃ麵が粘着したり、 乾燥に際して麵が 伸びたりする原因となる。 そのため生地ゃ麵が製麵 «に粘着する性質を減らし、 麵と 麵とが粘着する性質を減らし、 麵の重量を軽くしょうとカロ水率を低くする。 すると、 加 水率を低くしたためにダルテン組織の量が減って伸びやすくなり^ I環をきたす。 現在 用レ、られている攪拌混合型のミキサ一は、 旧来型のパッチタイプのミキサーも新型の連 水混合型のミキサーも、 大なり小なりこのような問題を抱えてレ、る。 Stirring and mixing when making flour into flour to make a dough for malting is a typical example of the prior art in which a liquid material is bound to a powder material. Stirring-mixing type mixers having various types of stirring blades and stirring bars have been used. However, even when 30 wt% to 40 wt% of water is added to barley flour as «^ dough is made, 40 wt% to 50 0 wt% like hand-made dough. It takes about 20 minutes to add water, and it takes time. Moreover, with stirring and mixing close to 20 minutes: It is not possible to make 3⁄47 Κ spread all over the wheat standing. 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. Between 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. More than that As stirring and mixing continues, 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 _ 、 | 哉 | to be destroyed is increased, but in the dough, the fibers of gluten which are excessively hydrolyzed or unhydrated are broken. Even if the water content is less than 50%, the dough may stick or wrinkles may develop during drying. As a result, the properties of the fabric and the stick will be reduced, the properties of the stick and the stick will be reduced, and the weight of the stick will be lightened and the water content will be reduced. Then, the amount of darten structure decreases and it becomes easy to grow by lowering the water supply rate, and I ring is generated. The mixing and mixing type mixer, which is currently used, and both the old patch type mixer and the new type of continuous water mixing type mixer have such problems with larger and smaller ones.
小麦粉に重量比 6 0 %以上の水や牛乳や卵などの水分を加えて製パン用の生地をつ くる攪拌混合も、 粉体原料と液体原料とを結合させる従来技術の典型的な例である。 加 水率が高く生地が柔らカ^、ので生成されたグルテンの糸 ii が攪掛昆合によつて破壌され る度合いは製麵用の生地つくりに比べれば少ないが、 τΚや牛乳の中でも小麦粉がだまを つくることからも明らかなように、 製麵用の生地に比べれば格段に加水率が高い製パン 用の生地つくりにおいても小麦粉の中の空気は水分の拡散を阻み、 小麦粉に水分を均一 にゆきわたらせるまでに少なからぬ時間を要する原因となっている。 小麦粉と水分が均 一化するまでの生地は粘着する性質が甚だしく、 攪裕昆合の時間が経過して水分が均一 になると生地が粘着する性質が減って滑らかになる。 製パン用の生地つくりにおいて原 料を攪拌する目的は、 水分を小麦粉全体にゆきわたらせることと、 その結果生じたダル テンを組織化するために担ねをおこなうことにある。 攪 ?昆合に要する時間のうち、 水 分を全体にゆきわたらせるために費やす時間の割合は大きレ、。 本願出!^者は、 小麦粉のように粒子力 s微細で、 そのため立子と ί子の間に微細な単 位の空気を多量に含む粉体原料に加水をおこなうに際しては、 当初に加水むらをつくる ことなく、 両者を当初から均等に結びつける加水をおこなうことが肝要で、 そのような 方法で加水をおこなうことによつて生地つくりや製麵が抱えてレ、る多くの問題を解決 することができるとして特願昭 4 7— 4 2 6 2 8を出願した。 Stirring and mixing the flour for bread making by adding water such as water at a weight ratio of 60% or more or water such as milk or egg to flour is also a typical example of the prior art in which powder raw material and liquid raw material are combined. is there. The degree to which the produced gluten yarn ii is broken by agitation and kneading because the water content is high and the dough is soft, is less in comparison with the production of the dough for making rice bran, but among 中 で も and milk As is clear from the fact that flour makes a dam, the air in the flour blocks the diffusion of water even in making a dough for bread making, which has a much higher water content than the dough for making a meal, and the moisture in the flour It takes a considerable amount of time to spread the The dough has a strong adhesive property until the flour and water become uniform, and when the agitation time passes and the water becomes uniform, the dough adhesive property decreases and becomes smooth. The purpose of agitating the ingredients in making bread dough is to spread the moisture throughout the flour and to carry it in order to organize the resulting dullene. Of the time required for agitation, the proportion of time spent to spread water throughout is large ,. This application is out! Those who do not have water unevenness at the beginning when hydrolyzing a powdery material that contains a large amount of fine air between fine and small pieces, such as wheat flour, are fine in particle power s. It is important to add water evenly from the beginning, and it is important to do so in such a way that it can solve many problems associated with dough making and iron making. I filed an application 4 7-4 2 6 2 8
その後、 この加水技術を擬似的に実用化する装置として、 日本製粉株式会社から小麦粉 力口水用のフロージエツター、 株式会社昭和産業から小麦粉加水用のタービュライザ、 日 清製粉株式会社から小麦粉加水用のスーパーターボカ湘次いで発売されて広く使用され るようになつた。 現在もその変开趣が供給されている。 After that, as a device to put this hydrolysis technology to practical use in a pseudo manner, a flow diverter for flour from Japan powder company, a turbulizer for flour addition from Showa Sangyo Co., Ltd., a super turbo for flour addition from Nisshin Flour Milling Co., Ltd. It was released next and became widely used. The change taste is supplied now.
小麦粉加水用のフロージェッタ一は、 株式会ネ: fc¾、研の加湿用フロージェッターを/ Jヽ 麦粉への加水に適するように改めたもので、 落下させた原料を微粒子化して接線方向に 飛ばす作用をする円盤の回 ISi度を速め、 円盤の周辺部に攪拌用のピンを多 ける改 造を施した装置である。 小麦粉への加水を連続化する上で有用な装置である。  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.
しかし、 次のような問題がある。 この装置において塩水などの液体原料は円盤上に筒状 に落下するので装置が水平に設置されてレ、れば液体原料は全円周方向に均等に飛ばされ る。 し力、し、 小麦粉は円盤の中心の辺りにただ落下させるだけなので中心の周囲に均等 に落下するわけではなく、 方向によって小麦粉が飛ばされる量に大きな差が生じる。 そのため小麦粉と: t^ などの液体原料はむらのある結合をして排出される。 However, there are the following problems. In this device, 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.
小麦粉のように粒子力 s微細でその粒子間に據する空気が水分の移動を阻む性質を持つ 粉体にこのような加水むらをつくると、 円盤の周辺のピンや羽根で攪拌してもこの加水 むらを容易に均一化することができなレ、。 そのためフロージェッターから排出後に別途 均一ィ匕を促がす擾拌混合をおこなわなければならなレ、。 さらに良質な生地を求めれば水 分の均一ィ匕を待っための寝かし熟成の工程を必要とする。 また、 この結合むら力 S原因で 小麦粉加水用のフロージエツターからは水分と未結合の小麦粉が漂レ、出るので髓装置 が必需品となる。 As in the case of flour, particle power s is fine, and the air between the particles has the property of blocking the movement of moisture. If such a water unevenness is formed in the powder, even if it is stirred with pins or blades around the disc Water can not be easily homogenized. Therefore, after discharging from the flow jetter, it is necessary to carry out stirring and mixing to promote uniform mixing separately. If you want a better quality fabric, water It requires a process of aging and aging to wait for a uniform amount of water. In addition, moisture and non-bonded flour float from the floe waterer for adding flour due to the binding unevenness S, and the straw device becomes a necessity because it comes out.
粉体原料と液体原料を同時に円盤上に落下させて微粒子ィ匕させるこの仕組みは、 パッチ タイプのミキサ一に用いることはできなレ、。 またこのタイプの装置は、 粉体原料と液体 原料の供給を開始する際と、 供給を停止する際に両原料を 中のような比率で供給す ることが困難なので少量の原料処理には向かなレ、。 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. In addition, 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.
小麦 、加水用のタービュライザは、 糸田川ミクロ ^式会社の連« ?昆合用のター ビュライザのパドルの回繊度を早めたもので、 小麦粉への加水を連続化する上で有用 な装置である。 し力し、 次のような問題がある。  Wheat, a turbulizer for water, Itogawa micro ^ formula company series «? This is an equipment that accelerates the fineness of the paddle of the turbulizer for kneading, and is a useful device for continuing the water addition to the wheat flour. There are the following problems.
円筒の一端の上部から供給される小麦粉が円筒内壁に沿って回転する間に小麦粉の供給 口に «して円筒上に設けられた' ¾ _Kノズルから ϋなどの液体原料が供給される。 そのため、 液体原料は ¾ζΚノズルの直下を通過する小麦粉に過剰に加えられる。 そして 直後に、 高速で回転するパドルによって微粒子ィ匕され、 未加水の小麦粉と攪掛昆合され て他端から排出される。 ノズルの直下で過剰な液体原料と結合して一^]口水むらを生じ た粉体原料は、 パドルで碎かれ、 その周囲に却口水の小麦粉を伴う状態になるが、 これ まで述べてきたように小麦粉の中の空気に水分の移動を阻まれるのでやはり容易には均 一化しない。 While the wheat flour supplied from the upper part of one end of the cylinder rotates along the inner wall of the cylinder, liquid raw material such as rice cake is supplied from the '3⁄4 K nozzle provided on the cylinder at the flour feeding port. Therefore, the liquid material is excessively added to the flour passing immediately below the 3⁄4ζΚ nozzle. Immediately after, it is fine-grained by a paddle rotating at high speed, mixed with unhydrolyzed flour and stirred, and discharged from the other end. The powdery material which is combined with the excess liquid raw material directly below the nozzle to create one uneven mouth is covered with a paddle and is accompanied by the flour of the spouted water around it, as described above. Also, the air in the flour blocks the movement of water, so it is not easy to equalize either.
この加水装置では、 小麦粉などの粉体原料を円筒内壁に層を形成するほど多量に供給す ると非常に効率が悪くなり、 両原料を均一に結合させることがますます困難になる。 ¾ΤΚノズルの下で などの液体原料と過剰に結合した小麦粉は、 攪拌羽根でたた力^ て微粒子ィ匕されても液体原料と結合して質量を増してレ、るので円筒内壁の側に留まろう とする。 一方、 ifeKと結合してレヽなレ、質量が小さな小麦粉は層の回転軸の側に留まろう とする。 このため層の内壁側の加水小麦粉と回転軸側の未加水小麦粉との混合が物理的 に拒まれるので液体原料の移動がますます進まなレヽ。 それゆえこの化袓みの装置では、 小麦粉が層を形成することがないように、 粉体原料は少量ずつ供給される。 しカゝし、 小 麦粉を少量ずつ供給しても加水むらは解消されずに排出されるので、 排出後に水分を均 ーィ匕させるための攪拌混合の工程を要し、 さらに良質な生地を求めればさらなる均一化 の進行を待っための寝かし熟成の工程を必要とする。 In this water supply apparatus, if a large amount of powdery raw materials such as wheat flour is supplied to form a layer on the inner wall of the cylinder, the efficiency becomes very poor, and it becomes more difficult to uniformly bond both raw materials. The flour bound with liquid ingredients such as under excess water is added to the liquid ingredients even if it is finely divided by the force of the stirring blade, and the mass is increased, so it is on the inner wall of the cylinder. Let's stay I assume. On the other hand, when combined with ifeK, it is easy to retain flour, which has a small mass, on the side of the axis of rotation of the bed. Because of this, mixing of the hydrolyzed flour on the inner wall side of the layer and the non-hydrolyzed flour on the rotary shaft side is physically refused, so the movement of liquid ingredients is progressing more and more. Therefore, in this apparatus, powder material is supplied little by little so that the flour does not form a layer. Because even if the wheat flour is supplied little by little, it can be discharged without eliminating the unevenness of water, so it requires an agitation and mixing process to equalize the water after discharge, and it is possible to make a better quality dough. If it is required, it will need a aging and aging process to wait for the progress of further homogenization.
この tb袓みは、 羽根の向きや、 粉体原料の投入口や、 、餘ノズルの数や、 結合物の取出 し口などを改めても、 粉体原料が層をつくるパッチタイプのミキサーとして用いること はできない。 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.
また、 このタイプの装置は、 粉体原料と液体原料の供給を開始する際と、 供給を停止す る際に両原料を稼動中のような比率で供給することが難しいので少量の原»理には向 かない。 In addition, 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
小麦粉加水用のスーパーターボは小麦粉加水用のタービュライザと基本的に同一な 装置である。 タービュライザの回転羽根がパドル状であるのに対して、 スーパーターボ の回転羽根は板状や丸棒状である。 タービュライザと同様な問題点があり、 タービユラ ィザと同様の理由でその b袓みをパッチタイプの装置に用いることはできず、 少量の原 料処理にも向かない。  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.
タ一ビュラィザやスーパーターボ型のミキサーを改良して、 回転軸を原料の供給端 のみで支えて駆動し、 円筒を排出端の健こ容易に取り外し、 清掃のための便宜性を高め た日本製粉のエンジニアリング部門が供給する HD連続加水混合装置 ·特開平 0 7— 3 2 7 5 7 5がある。 装置全体が小型化され、 清掃も容易になり有用なミキサーである。 しかし、 カロ水物が持つ問題点はタービュライザゃス一パーターボに準じ、 従って、 この ミキサ一で加水をしたあとで、 水分を均一化するために真空ミキサ一によつて攪拌処理 をおこなうことが推奨されている。パッチタイプへの応用が不可能な化組みである点も、 従来のタービュライザゃス一パーターボと変わらない。 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. There is an HD continuous water mixing device supplied by the engineering department of Japan · Japanese Patent Application Laid-Open No. 0 7-3 2 7 5 7 5. The entire system is miniaturized and easy to clean, making it a useful mixer. However, according to 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.
真空ミキサーと称されるミキサーが以前から供給されている。 容器内を脱気しなが ら攪拌混合をおこなうミキサーである。 粉体原料に含まれる空気の妨害を排して液体原 料を粉体原料の中に効率よく拡散 ·浸透させるのでミキシング時間も早く小麦粉へのカロ 水に用いればグルテンがよく組織される。 しかし、 このミキサーを用いて製造した食品 は、 食品としての味わレヽゃ風味を欠く。 ミキシングの過程で原料中の空気力 S排除され空 気を僅かし力含まなレ、食品になるので、 咀嚼する際に味蕾への味成分の刺激が連続的に なり、 人の味蕾の性質上、 食品の味や風味を感じ難いためである。 脱気して攪拌混合を おこなうミキサ一は食品製造用のミキサ一としては大きな欠陥を持つと言わざるを得な い。  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.
特許出願公開昭 6 3— 2 5 8 5 2 7は、 回転羽根から液体原料を加えるミキシング の技術である。 しカゝし、 羽根の先端部に噴出口を設けて注水すれば、 羽根の先端部にあ る粉体原料の中に水を注入することになる。 従って、 粉体原料に液体原料が過剰に加え られた部分をつくることを避けることができない。 この出願者はまた、 羽根の回転方向 と逆方向の位置に噴出口を設けて水を噴出させれば羽根の後部は負圧になるので水が霧 状になると言う。 羽根の後部には確かに渦流や乱流が生じ負圧が生ずる。 しかし、 水滴 が水滴であり続けようとする性質は強く、 攪拌羽根の渦流や乱流による負圧くらいで水 力 S微粒子化されることはなレ、。 羽根の後部から噴出された水が小さな水滴になることは あっても微粒子化されることはない。 小さな水滴は微細な粒子で構成される小麦粉にと つては巨大な水塊である。 単位の大小はあれ、 一且小麦粉に過剰に加水された部分をつ くつた上で、 これを提拌混合して困難な水分の拡散に挑戦しなければならなレヽ点は一般 的な攪拌混合型ミキサーと変わらなレ、。 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. However, 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.
特許出願公開昭 5 7— 1 3 6 9 2 5は、 回転軸上に設けた水の噴出口が回転するの で撒水装置のように水力 S微粒子化されると言う。 しかし、 «装置で水を撒き散らす力 くらいで水を微粒子化することはできない。 そもそも、 «装置は水を撒き散らしはす る力 S微粒子ィ匕しないようにした装置である。 もし 装置の水力 S微粒子化されるとすれ ば、 蒸発する水が増えて撒水効果は激咸する。 水のような互いに結びつこうとする性質 が強い液体は、 結びつきを維持しょうとする^^の液体を大きな加速度に曝して引きち ぎり分散させるような、 液体を微粒子ィ匕させる技術の »:を踏まえた手段によることな しには微粒子化を果たすことはできなレ、。 そこで本発明によつて次のような を解決する。  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. However, it is not possible to micronize water with the power of sprinkling it with the «device. In the first place, 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.
すでに述べてきたように、 小麦粉のように粒子力 S微細であるために粒子間に微細な 単位の空気を多量に含む粉体原料は、 一旦液体原料と過剰に結びついた部分をつくつて しまうと、 液体原料が粉体原料の中を拡散し浸透することを空気が妨げるために、 液体 原料を粉体原料に均等にゆきわたらせることが困難になり、 均一な結合を容易に果たす ことができない。 実用的な範囲の均一ィヒにも長い時間を要するばかりカゝ、 生成されたグ ルテン紙織が攪拌混合によって破壊される小麦粉などに加水をする には、 水を小麦 粉全体にゆきわたらせる目的自体を早い段階で放^ざるを得なくなる。  As described above, the powdery raw material containing a large amount of fine unit air between the particles because of the fineness of the particle power S such as wheat flour 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.
そこで、 小麦粉のように粒子力 S微細で粒子間に多量の空気を含む、 内部で液体原料を移 動させることが難しレ、粉体原料に、 水のように微粒子化が容易でなレ、液体原料を加えて 両原料を結合させるに際して、 過剰な結合部分をつくることな《 液体原料を微立子化 した上で粉体原料に加えることによって、 短時間のうちに均一な結合を果たし、 かつ、 力つてなく良質な結合物を得る方法を ί^ί共する。 しかも、 その方法は、 連続的なミキシ ングにも、 パッチタイプのミキシングにも、 また多量の原料のミキシングにも、 少量の 原料のミキシングにも用いることができる方法である。 発明の開示 Therefore, it is difficult to move 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. << By making the liquid raw material finely divided and adding it to the powder raw material, uniform bonding can be achieved in a short time, and the strength is excellent. How to get a good bond. Moreover, 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
円筒あるいは円筒に準ずる容器の内壁に沿って粉体原料を回転させる。 その際、 粉 体原料の層の内部における粉体原料と液体原料の結合物と未結合物の円筒内塑則と回転 軸側の移動を妨げる過大な加速度が生じることがないようにする。  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.
この粉体原料に対して回転軸の側から微粒子ィ匕した液体原料を加える。 The fine particle-like liquid material is added to the powder material from the side of the rotating shaft.
その液体原料を微粒子化する度合レ、とその単位時間当りの供給量を、 粉体原料の回転軸 側の表層に生ずる両原料の結合物の結合率が両原料の最終的な結合率を上回ることがな い結合率になるようにする。 The degree of atomization of the liquid raw material, and the feed rate per unit time, the binding rate of the combination of both raw materials produced on the surface side of the rotary shaft of the powder raw material exceeds the final binding rate of both raw materials Make sure that there is no chance of binding.
このようにして液体原料と過剰に結合した液体原料を粉体原料の中で結合の後に移動さ せたり拡散させたりすることを必要としなレ、結合をおこなう。 In this way, it is necessary to cause the liquid raw material and the liquid raw material excessively bound to be transferred or diffused in the powder raw material after bonding.
粉体原料が層を形成していれば、 層の回転軸側の表層で微粒子状の液体原料と結合して 質量を増した結合物は、 回転にともなレ、層の内壁の側に移動する。 代わつて回転軸側の 表層には液体原料と未結合の質料が小さレ、粉体原料が表れる。サイクロンの原理である。 結合が進んで全体が結合物になれば、 結合の度合レヽが少な!/ \ 質量が比較的小さな結合 物が回転軸側の表層に表れて微粒子状の液体原料と結合する。 この段階においては単位 時間当たりの微粒子状の液体原料の供給量を減らす。 粉体原料を円筒の内壁に沿って回転させるために、 先端部が内壁に沿って回転する粉体 原料に届き粉体原料に作用する回転羽根を設け、 粉体原料を内壁に沿って回転させるこ とができ、 力つ粉体原料を内壁に押付け過ぎることのなレ、加速度が生じる で羽根を 回転させる。 あるいは、 粉体原料に作用する羽根あるいは突起物を円筒の内壁に設け、 羽根あるいは突起物に、 粉体原料を内壁に沿って回転させることができ、 かつ、 円筒の 内壁に押付け過ぎることのなレ、加速度が生じる速度で円筒を回転させる。 If 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. 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. Alternatively, 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.
円筒の内壁に沿つて回転する粉体原料に液体原料を微粒子化して回転軸の側から加える ために、 先^ ¾あるレヽは側端部が内壁に沿って回転する粉体原料に届くことのなレ、羽根 を回転軸に設ける。 最終的な結合率を超える結合が表層部に生じることがないような供 給量で供給する液体原料を、 羽根の先 5¾¾が粉体原料に接していなければ羽根の先 力ら、 羽根の先端部が粉体原料に接して!/ヽれば側端部から放ち微粒子化させる。 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.
羽根の先 あるレヽは側端部に供給する液体原料をその供給量の下で微粒子化させるこ とができる加速度が生じる速度で羽根を回転させる。 粉体原料に作用する羽根や棒と液 体原料に作用する羽根を一体にすることも、 粉体原料に作用する羽根や棒と液体原料に 作用する羽根を別々にすることも、 あるいは両者の羽根を別々に βしてそれぞれに最 適な加速度が生じるように回転させることもできる。 後に述べるように、 両者の羽根を 另リ々に駆動する方法力 S機能的には最も好ましレヽ。 図面の簡単な説明 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. Brief description of the drawings
第 1図は粉体原料を円筒の内壁に沿って回転させる長レヽ羽根と、液体原料を微粒子 化して放つ短い羽根を同一の回転軸に設ける装置の原理を示す図である。  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.
内部を液体原料の通路、即ち供給管にした太い回転軸をはさんで対向する位置に、長い 羽根と短レヽ羽根を同一平面上に設けた装置の、 羽根と回転軸を含む面の断面図である。 液体原料は太レヽ回転軸の内部、即ち供給管から小穴を通つて短レ、羽根の前面下部に供給 される。 1 6頁の 3行目以下に述べる実施の形態の一例である。 It is long at the position where it faces the passage of liquid material inside, that is, the thick rotating shaft which made the supply pipe It is sectional drawing of the surface containing the blade | wing and rotation axis of the apparatus which provided the blade | wing and the short reed blade | wing 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 short portion and the lower front of the blade. This is an example of the embodiment described on the third line of page 16.
なお、 円筒に設ける粉体原料の投入口や、結合物の排出口は省略した。粉体原料を左や 右の方向に移動させる羽根の向きの変ィ匕なども省略した。羽根の前面下部に液体原料を 供給する穴は実際の割合より大きく描いてある。 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.
第 2図は、第 1図の a bを結ぶ線を含む面の、第 1図とは 9 0° 向きを変えた断面 図である。 点線は a bを結ぶ面から離れた位置にある羽根を示す。  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.
円筒の上部の矢印は長短の羽根の回転方向を示す。 The arrows at the top of the cylinder indicate the direction of rotation of the long and short blades.
第 3図は粉体原料を円筒の内壁に沿って回転させる羽根と、液体原料を微粒子化し て放つ羽根を別途駆動する装置の原理を示す図である。  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.
粉体原料を円筒の内壁に沿って回転させる羽根を回転軸をはさんで対向する位置に設 け、液体原料を微粒子化して放つ横に長い羽根を、 内部を液体原料の通路、即ち供給管 にした太い回転軸上に回転軸をはさんで対向する位置に 1ネ: つ、合計 2枚設けた装置 である。この装置の全ての羽根を同一平面上に位置するように停止させた状態における、 羽根と回転軸を含む面の断面図である。 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.
液体原料は太レヽ回転軸の内部、即ち供給管から小穴を通って羽根の前面下部に供給され る。 1 8頁の 9行目以下に述べる実施の形態の一例である。 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.
粉体原料に作用する羽根は、両フランジを結ぶ円筒内壁面に沿つた曲板に取付けられて いる。 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.
なお、 円筒に設ける粉体原料の投入口や、結合物の排出口は省略した。粉体原科を左や 右の方向に移動させる羽根の向きの変ィ匕なども省略した。羽根の前面下部に液体原料を 供給する穴は実際の割合より大きく描いてある。 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.
第 4図は第 3図の a bを結ぶ線を含む面の、第 3図とは 9 0° 向きを変えた断面図 である。 点 #泉は a bを結ぶ面から離れた位置にある羽根を示す。  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.
円筒の上部の矢印は粉体原料に作用する羽根と液体原料に作用する羽根の回転方向を 示す。 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.
第 5図は粉体原料を円筒の内壁に沿って回転させる円筒と、液体原料を微粒子化し て放つ羽根を另 IJ途駆動する装置の原理を示す。  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.
回転軸をはさみ対向する位置に羽根状の突起物を有する、粉体原料を円筒の内壁に沿つ て回転させる回転円筒の内部に、液体原料を微粒子化して放つ横に長い羽根を、内部を 液体原料の通路にした太!、回転軸上に回転軸をはさんで対向する位置に 1; ¾rfつ、合計Inside the rotary cylinder that has blade-like projections at opposite positions with the rotation axis and rotates the powder material along the inner wall of the cylinder, a laterally long blade that atomizes the liquid material and releases It was fat in the passage of liquid material! 1, 3⁄4 rf, total, in opposite positions across the rotation axis on the rotation axis
2枚設けた装置である。この装置の全ての羽根を同一平面上に位置するように停止させ た状態における、 羽根と回転軸を含む面の断面図である。 It is an apparatus provided with two sheets. 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.
液体原料は太レヽ回転軸の内部、即ち供給管から小穴を通って羽根の前面下部に供給され る。 1 9頁の 9行目以下に述べる実施の形態の一例である。 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.
なお、 円筒に設ける粉体原料の投入口や、結合物の排出口は省略した。粉体原料を左や 右の方向に移動させる羽根の向きの変ィ匕なども省略した。羽根の前面下部に液体原料を 供給する穴は実際の割合より大きく描いてある。 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.
第 6図は第 5図の a bを結ぶ線を含む面の、 第 5図とは 9 0 ° 向きを変えた断面 図である。 点線は a bを結ぶ面から離れた位置にある羽根を示す。  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.
円筒の上部の矢印は粉体原料に作用する羽根と円筒と液体原料に作用する羽根の回転 方向を示す。 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.
第 7図は回転軸に設けた羽根の先¾ ^で粉体原料を円筒の内壁に沿って回転させ、 同じ羽根の側端部から液体原料を微粒子ィ匕して放つ装置の原理を示す図である。 内部を液体原料の通路にした太レ、回転軸上に回転軸をはさんで対向する位置に複数の 羽根を設けた装置の羽根と回転軸を含む面の断面図である。 In FIG. 7, the powder material is rotated along the inner wall of the cylinder with the tip of the blade provided on the rotating shaft, It is a figure which shows the principle of the apparatus which carries out the microparticles | fine-particles discharge of the liquid raw material from the side edge part of the same blade | wing. 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.
液体原料は太い回転軸の内部、即ち供給管から小穴を通って羽根の前面下部に供給され る。 1 9頁の 1 4行目以下に述べる実施の形態の一例である。 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.
なお、 円筒に設ける粉体原料の投入口や、結合物の排出口は省略した。粉体原料を左や 右の方向に移動させる羽根の向きの変ィ匕なども省略した。羽根の前面下部に液体原料を 供給する穴は実際の割合より大きく描!/、てある。 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! /.
第 8図は第 7図の a bを結ぶ線を含む面の、第 7図とは 9 0° 向きを変えた断面図 である。 点線は a bを結ぶ面から離れた位置にある羽根の部分を示す。  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.
円筒の上部の矢印は羽根の回転方向を示す。 The arrow at the top of the cylinder indicates the direction of rotation of the blades.
第 9図は粉体原料を円筒の内壁に沿って回転させる の先 ¾¾¾を持ち、逆 の側端部から液体原料を微粒子ィ匕して放つ羽根を回転軸に設けた装置の原理を示す図 である。  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.
内部を液体原料の通路にした太レヽ回転軸をはさんで、対向する位置に羽根を並べた装置 の羽根と回転軸を含む面の断面図である。 It is sectional drawing of the surface containing the blade | wing of the apparatus which arranged the blade | wing in the position which opposes on both sides of the thick-wafer rotational axis which made the inside the channel | path of liquid raw material, and a rotational axis.
液体原料は太い回転軸の内部、即ち供給管から小穴を通って羽根の逆 V 型の側端部の 前面下部に供給される。 2 0頁の 1 1行目以下に述べる実施の形態の一例である。 なお、 円筒に設ける粉体原料の投入口や、結合物の排出口は省略した。粉体原料を左や 右の方向に移動させる羽根の向きの変ィ匕なども省略した。羽根の前面下部に液体原料を 供給する穴は実際の割合より大きく描いてある。 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. This is an example of the embodiment to be described on line 1 on 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.
第 1 0図は第 9図の a bを結ぶ線を含む面の、第 9図とは 9 0 ° 向きを変えた断面 図である。 点線は a bを結ぶ面から離れた位置にある羽根と羽根の部分を示す。 円筒の上部の矢印は羽根の回転方向を示す。 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.
第 1 1図は粉体原料を円筒の内壁に沿って回転させる棒状の先 を持ち、粉体原 料に届くことのなレ、低レ 置に第二の先 を持ち、低レ、位置の先 5¾¾から液体原料を 微粒子化して放つ多段式の羽根を回転軸に設ける装置の原理を示す図である。  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.
内部を液体原料の通路にした太レ、回転軸をはさんで、対向する位置に多段式の羽根を並 ベた装置の羽根と回転軸を含む面の断面図である。 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.
液体原料は太い回転軸の内部、即ち供給管から小穴を通って羽根の第二の先^ ¾の前面 下部に供給される。 2 0頁の 2 2行目以下に述べる実施の形態の一例である。 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.
なお、 円筒に設ける粉体原料の投入口や、結合物の排出口は省略した。粉体原料を左や 右の方向に移動させる羽根の向きの変ィ匕なども省略した。羽根の前面下部に液体原料を 供給する穴は実際の割合より大きく描いてある。 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.
第 1 2図は第 1 1図の a bを結ぶ線を含む面の、第 1 1図とは 9 0。 向きを変えた 断面図である。 点線は a bを結ぶ面から離れた位置にある羽根を示す。  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.
円筒の上部の矢印は羽根の回転方向を示す。 符号の説明  The arrow at the top of the cylinder indicates the direction of rotation of the blades. Explanation of sign
1 円筒  1 cylinder
2 内部が液体原料の供給管を構成する、粉体原料に作用する回転羽根と液体原料を 微粒子化する回転羽根を取付けた太レヽ回転軸部  2 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
3 粉体原料に作用する回転羽根  3 Rotary blade acting on powder material
4 液体原料を微粒子化する回転羽根 5 液体原料を羽根の前面に供給する供給穴 4 Rotary vanes to atomize liquid raw materials 5 Supply holes for supplying liquid material to the front of the blade
6 羽根を取付けた太い回転軸部内の供給管に液体原料を円筒外部から導入する回 転軸内部の供給管  6 Feed pipe inside the rotary shaft that introduces liquid material from the outside of the cylinder into the feed pipe inside the thick rotary shaft part to which the blades are attached
11 円筒 11 cylinder
12 内部力 S液体原料の供給管を構成する、 液体原料を微粒子化する回転羽根の回転 軸部 12 Internal force S Rotary shaft part of the rotating blade that atomizes the liquid material, which constitutes the supply pipe of the liquid material
13 粉体原料に作用する回転羽根  13 Rotary Blades Acting on Powder Material
14 液体原料を微粒子化する回転羽根 14 Rotary vanes to atomize liquid raw materials
15 液体原料を羽根の前面に供給する供給穴 15 Supply hole for supplying liquid material to the front of the blade
16 羽根を取付けた太い回転軸部内の供給管に液体原料を円筒外部から導入する回 転軸内部の供給管 16 Feed pipe inside the rotary shaft that introduces liquid material from the outside of the cylinder into the feed pipe inside the thick rotary shaft with the blades attached
17 粉体原料に作用する回転羽根の回転軸 17 Rotary shaft of the rotating blade acting on the powder material
18 粉体原料に作用する回転羽根を取付ける曲板を取付ける回転軸のフランジ 19 粉体原料に作用する回転羽根を取付けるための両フランジを結ぶ曲板  18 A flange of a rotating shaft for mounting a curved plate for mounting a rotary blade acting on a powder material 19 A curved plate connecting both flanges for mounting a rotary blade for acting on a powder material
20 液体原料を微粒子化する回転羽根の回転軸 20 Rotary shaft of the rotating blade that atomizes the liquid material
21 回転する円筒 21 Rotating cylinder
22 内部が液体原料の供給管を構成する、液体原料を微粒子化する回転羽根を取付け た太い回転軸部  22 A thick rotary shaft attached with a rotating blade that atomizes the liquid material, the inside of which constitutes the supply pipe for the liquid material
23 円筒内壁面に取付けられた粉体原料に作用する回転羽根 23 Rotary vanes acting on the powder material attached to the inner wall of the cylinder
24 液体原料を微粒子化する回転羽根 24 Rotary vanes to atomize liquid raw materials
25 液体原料を羽根の前面に供給する供給穴  25 Supply hole for supplying liquid material to the front of the blade
26 羽根を取付けた太レ、回転軸部内の供給管に液体原料を円筒外部から導入する回 転軸内部の供給管 26 Large diameter with a blade attached, for introducing liquid material from the outside of the cylinder to the supply pipe in the rotating shaft Supply pipe inside the rotary shaft
27 円筒の回転軸  27 Axis of rotation of cylinder
31 円筒 31 cylinder
32 内部が液体原料の供給管を構成する、 回転羽根を取付けた太い回転軸部 33 粉体原料に作用する回転羽根の先驗  32 A thick rotary shaft with rotating blades attached, the inside of which constitutes a supply pipe for liquid material 33 The tip of a rotating blade acting on powder material
34 液体原料を微粒子化する回転羽根の側端部  34 Side edge of the rotating blade that atomizes the liquid material
35 液体原料を羽根の前面に供給する供給穴 35 Supply holes for supplying liquid material to the front of the blade
36 羽根を取付けた太い回転軸部内の供給管に液体原料を円筒外部から導入する回 転軸内部の供給管  36 Supply pipe inside the rotary shaft that introduces liquid material from the outside of the cylinder into the supply pipe in the thick rotary shaft part to which the blades are attached
41 円筒 41 cylinder
42 内部力 S液体原料の供給管を構成する、 回転羽根を取付けた太い回転軸部 43 粉体原料に作用する回転羽根の先  42 Internal force S A thick rotary shaft attached with a rotating blade that constitutes the supply pipe for the liquid material 43 Tip of the rotating blade acting on the powder material
44 液体原料を微粒子化する回転羽根の側端部 44 Side edge of the rotating blade that atomizes the liquid material
45 液体原料を羽根の前面に供給する供給穴 45 Supply hole for supplying liquid material to the front of the blade
46 羽根を取付けた太!/ヽ回転軸部内の供給管に液体原料を円筒外部から導入する回 転軸内部の供給管 46 Inserting the liquid material from the outside of the cylinder into the feed pipe in the thick-blade / spindle-rotating shaft with a blade attached The feed pipe inside the rotary shaft
51 円筒 51 cylinder
52 内部が液体原料の供給管を構成する、 回転羽根を取付けた太い回転軸部 53 粉体原料に作用する、 回転羽根の先赚 15  52 Inside constitutes supply pipe of liquid material, thick rotary shaft with rotating blades attached 53 Working on powder material, tip of rotating blades 15
54 液体原料を微粒子化する、 回転羽根の先驗! 5 54 Convert liquid raw materials into fine particles, the tip of the rotating blades! Five
55 液体原料を羽根の前面に供給する供給穴 55 Supply hole for supplying liquid material to the front of the blade
56 羽根を取付けた太い回転軸部内の供給管に液体原料を円筒外部から導入する回 転軸内部の供給管 発明を実施するための最良の形態 56 A procedure to introduce the liquid material from the outside of the cylinder into the feed pipe in the thick rotary shaft with the blades attached Feed tube inside a rotary shaft-Best mode for carrying out the invention
第 1図と第 2図にその原理的な装置の一例を示すように、 粉体原料を内壁に沿つて 回転させる長い羽根と、 液体原料を微粒子化する短い羽根を同一の回転軸に設け、 後者 で微粒子化した液体原料を内壁に沿って回転する粉体原料に回転軸の側から加える形態 である。  As shown in FIGS. 1 and 2 as an example of the apparatus in principle, 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.
粉体原料を円筒 1の内壁に沿って回転させるために、 内壁に沿って回転する粉体原料に その先端部が届く羽根 3などを円筒内の回転軸 2から立上げる。 また、 液体原料を微粒 子化するために、 羽根の先端部が粉体原料に届くことがなレヽ羽根 4などを同一の回転軸 から立上げ、 羽根の先 から液体原料を放って微粒子化する。 羽根 3などの先 に 粉体原料を内壁に沿って回転させることができるカロ速度が生じ、 力つ羽根 4などの先端 部に液体原料を微粒子ィ匕させることができるカロ速度が生じる速度で羽根を回転する。 以下に記すことは第 3図以下の形態にも共通する事柄である。 In order to rotate the powder material along the inner wall of the cylinder 1, raise the blade 3 or the like whose tip can reach the powder material rotating along the inner wall from the rotary shaft 2 in the cylinder. Also, in order to make the liquid material into fine particles, raise the blade 4 etc. from which the tip of the blade can reach the powder material from the same rotation axis, and release the liquid material from the tip of the blade to make it fine. . At the tip of the blade 3 etc., the caro speed that can rotate the powder raw material along the inner wall is generated, and at the speed of the carot speed that can make the liquid raw material fine particles at the tip of the force blade 4 etc. Rotate. What is described below is a matter common to the embodiment shown in FIG.
粉体原料に作用する羽根と液体原料に作用する羽根を同一の回転軸に設ける 、 粉体 原料に作用する羽根 3などの先 には粉体原料を内壁に沿って回転させるには十:^! ぎる加速度が生じる。 粉体原料を内壁に沿って回転させる羽根' 3などの作用が強すぎる と粉体原料が内壁に強く押付けられて、 液体原料と結合して質量を増した結合物が層の 内壁の健こ移動し、 代わって未結合の粉体原料が回転軸の側に表れる結合物と未結合物 の層内部での移動が妨げられる。 粉体原料への作用を減ずる手段としては粉体原料に作 用する羽根を丸 にしたり、 羽根を粉体原料に正対させないなどの手段を講じる。 羽根 4などの先^ ¾5に液体原料を供給するには、 図に示すように回転軸 2の内部に液体 原料の通路すなわち供給管を設けて回転軸に穿った小穴ゃスリット 5から羽根の前面に 液体原料を供給する方法がある。 液体原料は大きな加 «の下で羽根の前面で薄幕状に なり先端部に到達した僅かな部分ごとに先 15を离 I Lる。 従って、 羽根の先離に十分 な加速度が生じてレ、れば、 先端部を離れる液体原料は微粒子ィ匕される。 The blade acting on the powder material and the blade acting on the liquid material are provided on the same rotary shaft. The tip of the blade 3 acting on the powder material, etc. 10 to rotate the powder material along the inner wall ! 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. As a means to reduce the effect on the powder raw material, take measures such as rounding the blade acting on the powder raw material or preventing the blade from facing the powder raw material. In order to supply the liquid material to the tip ^ 3⁄45 of the blade 4 etc, the liquid inside the rotary shaft 2 as shown in the figure There is a method of supplying a liquid material to the front of the blade from a small hole or slit 5 formed in the rotation shaft by providing a passage for the material, ie, a supply pipe. The liquid material thins at the front of the blade under a large amount of heat and cuts the tip 15 for every small portion reaching the tip. Therefore, a sufficient acceleration occurs at the tip of the blade, and if this occurs, the liquid material that leaves the tip end is finely divided.
液体原料の供給の仕方は、 この図に示す方法に限らず、 回転軸上に設けた導管から羽根 の前面に供給する方法や、 液体原料を羽根の中を通って先端部まで導き先驗 15に設けた スリツトから分散させる、 羽根の内部をこの図の羽根の前面と同様に機能させる方法な ど様々ある。 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.
それぞれの羽根の数や、形状や、回転軸に取付ける位置や、回転軸への取付け方などは、 円筒の形状や、 処理する原料の性質や、 «\ 装置力 S連続型カパッチタイプかなどによ つてここで述べた条件の範囲にぉレ、て様々な形態が考えられる。 The number of blades, the shape, the position of mounting on the rotary shaft, the method of mounting on the rotary shaft, etc., the shape of the cylinder, the nature of the raw material to be processed, «\ Device force S continuous type patch type etc Therefore, various forms can be considered within the scope of the conditions described here.
たとえば、 粉体原料に作用する羽根と液体原料に作用する羽根を回転軸の幅いっぱいに 角度を変えて交互に多数設けることもできる。 連続型の:^は円筒内壁の粉体原料に作 用する羽根を、粉体原料を供給口から排出口に移動させることができるように配置する。 前半で液体原料を加え、 後半で捏ねをおこなう構造にすることもできる。 For example, 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. Continuous type: ^ arranges the blade acting on the powder material on the inner wall of the cylinder so that the powder material can be moved from the supply port to the discharge port. The liquid raw material can be added in the first half, and the structure can be made in the second half with kneading.
粉体原料に液体原料を加える度合!/ヽを粉体原料の投入口から排出口に向かつて進行する に従って減じるように変ィ匕させて排出口付近ではグルテンを組織するための捏ねのみを おこなうようにすることもできる。 羽根の形状もそれぞれの段階に応じてその働きに最 も適したものに変化させることができる。 従って、 一部の粉体原料に過剰な液体原料を カロえてから攪拌混合して均一ィ匕しょうとする従来の連続型のミキサーと異なり、 内壁に 沿つて回転する未結合の粉体原料あるレ、は結合度合レ、低レ、粉体原料が優先的に表れる回 転軸側の表面に対して微粒子状の液体原料を適量ずつ連続的に加えるので、 ヽ時間で 均一な結合物を得る。 How much liquid material is added to powder material! / It is also possible to convert rice bran so that it decreases as it advances from the inlet to the outlet of the powder material, and to perform only kneading to organize gluten near the outlet. The shape of the blade can also be changed to the one most suitable for its operation according to each stage. Therefore, unlike a conventional continuous mixer in which excess liquid material is added to part of the powder material and then stirred and mixed to achieve uniform mixing, there is an unbonded powder material that rotates along the inner wall. Since the fine particle liquid material is continuously added to the surface on the rotary shaft side where the powder material appears preferentially, the bonding degree A homogeneous bond is obtained.
パッチタイプの には、 容器内に粉体原料を投入し、 羽根を回転させて粉体原料が円 筒の内壁に沿つて回転する層を形成するのを待ち、 液体原料を微粒子化する羽根の先端 部に液体原料を微粒子ィヒできる加速度が生ずるのを待って液体原料の供給を開始する。 パッチタイプの装置で小麦粉などに加水する齢には、加水が完了した直後に羽根の速 度を減じて捏ねに転じる。 In the patch type, 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.
円筒や容器は横型でも隱でもよい。 円筒や織が横型のときには回転軸は横になり、 のときには回転軸も縦になる。 The cylinder and container may be horizontal or bowl-shaped. When the cylinder or weave is horizontal, the axis of rotation is horizontal, and the axis of rotation is also vertical when.
第 3図と第 4図にその原理的な装置を示すように、 粉体原料を内壁に沿って回転さ せる羽根と、 液体原料を微粒子化する羽根をそれぞれ別途屠離する回転軸に設け、 それ ぞれの羽根の機能に最も適した速度でそれぞれの羽根を回転させて、 : iiな状態に微粒 子化させた液体原料を、 内壁に沿つて最適な速度で回転する粉体原料に回転軸の側から 加える形態である。 この発明を最も効果的に実施することができる形態である。  As shown in Fig. 3 and Fig. 4 the principle of the apparatus, 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.
粉体原料を円筒 1 1の内壁面に沿って回転させるために、 円筒内部の両側端に沿って回 転軸 1 7にフランジ 1 8を設け、 両フランジの間に内壁に沿って回転する曲板 1 9をわ たす。 この曲板に粉体原料に作用する羽根 1 3などを設ける。 粉体原料を円筒 1 1の内 壁に沿って回転させることができるカロ速度が羽根 1 3などに生ずる速度でこの羽根 1 3 などを回転させる。 In order to rotate the powder material along the inner wall surface of the cylinder 11, 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.
液体原料を微粒子化するために、 羽根の先^ ¾が内壁に沿つて回転する粉体原料に届く ことがな!/ヽ羽根 1 4を嫌己の回転軸 1 7とは別途駆動する回転軸 1 2に設けその先 に液体原料を微粒子ィ匕させることができるカロ速度が生ずる速度で羽根 1 4などを回転さ せる。 羽根 1 4などに液体原料を適量ずつ供給して羽根の先端部から放って微粒子化する。 第 3図と第 4図の装置では、 回転軸に沿って横に長レ、一続きの羽根を回転軸をはさんで 各 1本ずつ合計 2本備えるが、 長い羽根でなくても、 また 2本の羽根でなくてもよレ、。 この形態にぉレ、ては液体原料を微粒子化する羽根 1 4などを必要に応じて十分に高速で 回転させることができるので、 液体原料を微粒子化する も、 液体原料を単位時間当 たりに供給する量も、 必要に応じた最適な状態に調節することができる。 In order to atomize the liquid material, 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. Supply a proper amount of liquid raw material to the blade 14 etc. and release it from the tip of the blade to make it into fine particles. In the devices shown in FIGS. 3 and 4, 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. In this mode, since 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.
羽根の形状や数、 取付け方、 液体原料の供給の仕方、 連続型やパッチタイプの構造と機 能のさせ方などは第 1図と第 2図にっレヽて記した内容に準じる。 The shape and number of the blades, how to attach them, how to supply the liquid material, and how to make the structure and function of the continuous type and patch type, etc. conform to the contents described in Figure 1 and Figure 2.
第 5図と第 6図の装置は、 基本的には第 3図と第 4図の装置と同じである。  The devices of FIGS. 5 and 6 are basically the same as the devices of FIGS. 3 and 4.
粉体原料を円筒 2 1の内壁に沿って回転させる手段として、 第 3図と第 4図の装置が回 転軸からフランジと曲板を介して設けた粉体原料に作用する羽根を用いるのに対して、 円筒 2 1そのものを回転させてこの円筒の内壁に粉体原料に作用する羽根あるいはこれ に代わる突起物を設ける形態である。 As means for rotating the powder material along the inner wall of the cylinder 21, 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. On the other hand, 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.
第 7図と第 8図は、 回転軸に設けた羽根の先端部で粉体原料を円筒の内壁に沿つて 回転させ、 同一の羽根の側端部から液体原料を放って微粒子ィ匕させ、 円筒の内壁に沿つ て回転する粉体原料に微粒子ィ匕された液体原料を回転軸の側から加える形態の原理的な 装置である。  In Figs. 7 and 8, the powder material is rotated along the inner wall of the cylinder at the tip of the blade provided on the rotary shaft, the liquid material is released from the side end of the same blade, and the particles are mixed. It is a principle device of the form in which the liquid raw material which is finely divided into the powder raw material rotating along the inner wall of the cylinder is added from the side of the rotating shaft.
羽根の回転方向に羽根の前面が正対し、 カゝっ羽根が回転軸の長さの方向に対して垂直に 立上がると、 羽根の前面の付根に供給する液体原料は遠心力によって粉体原料が接して Vヽる羽根の先端部に向かつて移動して微粒子ィ匕されることなく粉体原料に加えられる。 そこで、 羽根の前面を移動する液体原料を一方の側 に導き側驗 3 4から放ち微粒 子化するために、 側端が回転軸の長さの方向に対して鋭角をなすように立上げる。 但し、 液体原料を放つのは円筒の内壁側の側端部なので、 内壁側の側端のみが回転軸の 長さの方向に対して鋭角をなせばよい。 羽根の前面のィ 艮付近に供^ 1 "る液体原料を側 端部に導く方法は、 たとえば羽根の向きを回転の方向に対-して斜めを向くようにするな どの方法もあるが、 第 7図と第 8図のように内壁側の側端を回転軸の長さの方向に対し て鋭角をなすように設ける方法は液体原料を側端部に確実に導く方法の一つである。 羽根の先端部 3 3などに粉体原料を円筒 3 1の内壁に沿って回転させることができる加 速度が生じ、 力り側 4などに側端部から放つ液体原料を微粒子化させることがで きる加速度が生じる速度で羽根を回転させる。 When the front surface of the blade faces the rotation direction of the blade and the caulking blade rises vertically to the direction of the length of the rotation shaft, 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. There is also a 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. There is an acceleration that allows the powder material to be rotated along the inner wall of the cylinder 31 at the tip end portion 3 of the blade, etc., and the liquid material released from the side end portion at the force side 4 etc. Rotate the blades at a speed that produces a possible acceleration.
羽根の形状や数、 取付け方、 液体原料の供給の仕方、 連続型やパッチタイプの構造と機 能のさせ方などは第 1図と第 2図にっレヽて記した内容に準じる。 The shape and number of the blades, how to attach them, how to supply the liquid material, and how to make the structure and function of the continuous type and patch type, etc. conform to the contents described in Figure 1 and Figure 2.
第 9図と第 1 0図にその原理的な図を示す装置は、 回転軸に設けた羽根の先端部に 粉体原料を内壁に沿って回転させる加速度が生じ、 力 同一の羽根の側 |5に側端部か ら液体原料を放つて微粒子ィ匕させるカロ速度を生じさせて、 内壁に沿って回転する粉体原 料に微粒子化された液体原料を回転軸の側から加える形態の例である。  In the device whose principle is shown in FIGS. 9 and 10, 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. An example of a form in which the liquid raw material is released from the side end to generate a caro speed causing fine particles to be generated, and the finely divided liquid raw material is added to the powder raw material rotating along the inner wall from the rotary shaft side. It is.
羽根の前面の付根に供給する液体原料を羽根の片側あるいは両側の側 に導くガイド を羽根の前面に設けるなど、 液体原料を側端部に導く を有することを糊敫とする.。 この図の装置では羽根の中央部が柱状に盛上げてあるので、 羽根の前面の付根に供給さ れた液体原料は逆 V字形の側端部に導かれる。 羽根の中や羽根の表面に設けた導管を通 じて液体原料を直接に側端部に導くこともできる。 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. In the device shown in this figure, since the center of the blade is raised in a column, 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.
羽根の形状や数、 取付け方、 液体原料の供給の仕方、 連続型やパッチタイプの構造と機 能のさせ方などは第 1図と第 2図にっレ、て記した内容に準じる。 The shape and number of the blades, how to mount them, how to supply the liquid material, and how to make the structure and function of the continuous type and patch type, etc. conform to the contents described in Figure 1 and Figure 2.
第 1 1図と第 1 2図にその原理的な図を示す装置は、 羽根の先端都に粉体原料を 内壁に沿って回転させるカロ速度が生じ、 カゝっその羽根の回転軸寄りに円筒内壁の粉体原 料に届くことのなレヽ他の先離を設けてこの先 ¾に液体原料を放って微粒子化する加 速度を生じさせ、 円筒内壁に沿つて回転する粉体原料に微粒子化した液体原料を回転軸 の側から加える形態の例である。 液体原料を粉体原料に接することのない先 5¾¾に導く ガイドを設けるなど、 液体原料が粉体原料に接することのなレ、先 [5に進み、 粉体原料 が接する先端部に進むことがなレヽ構造にする。 この図の装置では羽根の中央部が柱状に 盛上がっているので羽根の前面の付根に供給された液体原料は粉体原料に接してレ、なレ、 先 3¾¾に導かれる。 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. It is an example of an embodiment in which 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. For example, by providing a guide that guides the liquid material to a point where it does not touch the powder material, the liquid material may come into contact with the powder material. Make it a simple structure. In the apparatus shown in this figure, since the central part of the blade is in the form of a column, 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.
羽根の形状や数、 取付け方、 液体原料の供給の仕方、 連続型やパッチタイプの構造と機 能のさせ方などは第 1図と第 2図につ!/、て記した内容に準じる。 既に記した発明の効果に ϋ¾する The shape and number of the blades, how to mount them, how to supply the liquid material, and how to make the structure and function of the continuous type and patch type, etc. conform to the contents shown in Fig. 1 and Fig. 2. Investigate the effects of the invention described above
これまで 2 0分近くの時間を要した 5 0 %以下の加水をおこなう製麵用の生地をつ くるミキシング時間が 3 0秒以内に短縮され、 しかもその生地はこれまでのように加水 むらを解消するためのさらなる攪拌混合や寝かし熟成を必要としない、 均一ィ匕がすでに 達成された生地である。  The mixing time to reduce the amount of water used to make the dough for watering up to 50% or less, which has taken nearly 20 minutes, has been reduced to within 30 seconds, and the dough has been unevenly hydrated as before. It is a dough for which uniform texture has already been achieved without the need for further stirring, mixing and aging to eliminate it.
これまで 5分以上の時間を要した 6 0 °/0以上の加水をおこなう製パン用の生地をつ くる際の水分を均一化するまでのミキシング時間が 3 0秒以内に短縮された。 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.
また、 結合むらをつくつてからこれを均一化する従来の粉体原料に刘する液体原料 の加え方と異なり、 本発明の粉体原料に機能する羽根と液体原料に機能する羽根を別々 に駆動する機構を用いれば、 粉体原料の状況に応じて液体原料を微粒子化する度合いを 変え、 単位時間当たりの液体原料の供給量を変えながら、 結合むらを生じさせることな く液体原料と粉体原料を結合させるので、 これまで困難であった微細な粉体原料に少量 の液体原料を均一に結合させることが容易に実現できるようになった。 Also, unlike the method of adding the liquid material to the conventional powder material to make the bonding unevenness and then uniform it, 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.
また、 この発明の方法を活用すれば、 結合させる原料の性質ごとに異なる な結 合のさせ方を組立て、 また、 求める結合物の性質をつくりだすために最 な結合のさせ 方を組立てて両原料を結合させることが可能になった。  In addition, if 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
この粉体原料に対する液体原料の加え方は、 無重力の下におレ、ても高レ、効率を維持 しておこなうことができる。 産業上の利用可能性  The liquid raw material can be added to the powder raw material under weightlessness, even with high efficiency and maintaining high efficiency. Industrial applicability
粉体原料力 S微粒子状でその粒子間に気体を含み、 そのため液体原料を加えるミキシ ングが容易ではなレヽ粉体原料と液体原料のミキシングは、 産業の広レヽ分野でおこなわれ ている。 改善の効果が劇的に大きく、 の形態が単純で実用化力 S容易なこの技術は、 産業上の利用可能性が高い。  Powder raw material power S 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.
国際出願番号 P C T/ J P 0 3 /0 0 7 1 1の出願技術と組み合わせて用いれば、 力つてなくうまみ豊かで高品質な茹で上げたパスタや 類を、 原料粉から 1分以内で製 造する画期的な製麵装置を実現することができる。  When used in combination with the application technology of International Application No. PCT / JP 0 3/0 0 7 1 1, it produces forcelessly rich, high-quality boiled pasta and dishes from raw material powder in less than 1 minute. It is possible to realize a revolutionary steel making device.

Claims

請 求 の 範 囲 The scope of the claims
1 . 粉体原料を円筒の內壁に沿って回転させて、 微粒子化させた液体原料を回転軸の側 から加える粉体原料に対する液体原料-の加え方。 1. How to add liquid material to powder material by rotating powder material along the wall of cylinder and adding micronized liquid material from the side of rotating shaft.
2 . 粉体原料を円筒の内壁に沿つて回転させる先 ¾¾5力 S粉体原料に届く羽根あるレ、は习习 根に準じる棒など (本請求の範囲において、 以降、 羽根あるいは羽根に準じる棒な どを、 羽根と称する) を回転軸に設け、 液体原料を羽根の先端部あるいは側 ¾か ら放って微粒子化させる先端部あるいは側^ ¾が粉体原料に届くことのなレヽ羽根を 回転軸に設け、 前者の羽根の先端部に粉体原料を円筒の内壁に沿って回転させる加 速度が生じ、 力 後者の羽根の先端部あるレ、は側端部から放つ液体原料を微粒子化 させる加速度が後者の羽根の先端部あるいは側端部に生じる速度で羽根を回転させ る。 この みによつて円筒の内壁に沿って回転する粉体原料に微粒子ィヒした液体 原料を回転軸の側から加える粉体原料に対する液体原料の加え方。  2. The powder material is rotated along the inner wall of the cylinder 3) The force with the blade that reaches the powder material is a rod with a blade that conforms to a ridge, etc. (In the following claims, the blade with a blade or a rod The blade is installed on the rotary shaft, and the tip or side of the liquid material is released from the tip or side of the blade to make it fine. In the former, there is an acceleration that rotates the powder material along the inner wall of the cylinder at the tip of the former blade, and the force at the tip of the latter blade is the acceleration that atomizes the liquid material released from the side edge. Rotates the blades at a speed that occurs at the tip or side end of the latter. Thus, the method of adding the liquid material to the powder material is added from the side of the rotation shaft to the powder material that is finely divided into the powder material that rotates along the inner wall of the cylinder.
3. 粉体原料を円筒の内壁に沿って回転させる先離! 5が粉体原料に届く羽根を回転軸に 設けて粉体原料を内壁に沿って回転させるカロ速度が先端部に生じる速度で羽根を回 転させ、 一方、 液体原料を羽根の先 あるいは側¾¾から放って微粒子化する先 端部あるいは側端部が粉体原料に届くことのない羽根を粉体原料に作用する羽根の 回転軸とは別途駆動する回転軸に設け、 习习根の先 |5あるレ、は側¾¾から放つ液体 原料;^微粒子ィヒされるカロ速度が生じる速度で羽根を回転させる。 この仕組みによつ て円筒の内壁に沿つて回転する粉体原料に微粒子化した液体原料を回転軸の側から 加える粉体原料に対する液体原料の加え方。  3. Allowing the powder material to rotate along the inner wall of the cylinder! 5 The blade reaching the powder material is attached to the rotary shaft, and the speed at which the powder material is rotated along the inner wall is generated at the tip. At the same time, the liquid material is released from the tip or side of the blade to make it into fine particles. The tip end or side end does not reach the powder material. The shaft is provided on a rotating shaft that is driven separately, and the reed of the root of the ridge is a liquid that is released from the side material. According to this mechanism, the method of adding the liquid material to the powder material is added from the side of the rotation shaft to the finely divided liquid material to the powder material rotating along the inner wall of the cylinder.
4. 粉体原料を円筒の内壁に沿って回転させる羽根や突起物を内壁に設け、 粉体原料を 内壁に沿って回転させる加速度が羽根や突起物に生じる速度で円筒を回転させ、 一 方、 液体原料を羽根の先端部ある V、は側端部から放つて微粒子化させる先端部ある Vヽは側端部力粉体原料に届くことのなレ、羽根を円筒の回転軸とは別途駆動する回転 軸に設け、 羽根の先端部あるレ、は側端部から放つ液体原料を微粒子化する加速度が 先端部あるいは側 5¾¾に生じる速度で羽根を回転させる。 この みによって円筒 の内壁に沿って回転する粉体原料に微粒子ィ匕した液体原料を回転軸の側から加える 粉体原料に财る液体原料のカロえ方。 4. Provide a blade or protrusion on the inner wall to rotate the powder material along the inner wall of the cylinder, The cylinder is rotated at a speed at which the acceleration caused by the rotation along the inner wall causes the blades and projections to rotate the cylinder, while the liquid source is V at the tip of the blade, V at The blade is installed on the rotary shaft which is driven separately from the rotary shaft of the cylinder, and the blade with a tip at the blade is an acceleration that atomizes the liquid material released from the side end. Rotate the blades at a speed that occurs at the tip or side 53⁄4. The liquid raw material finely divided into the powder raw material rotating along the inner wall of the cylinder by this alone is added from the side of the rotating shaft How to carry out the liquid raw material covering the powder raw material.
5 . 粉体原料を円筒の内壁に沿って回転させる先 ί驗! ^粉体原料に届き、 液体原料を放 つ側端部が回転軸の長さの方向に対して鋭角をなす羽根を回転軸に設け、 羽根の先 に粉体原料を円筒の内壁に沿って回転させるカロ速度が生じ、 かつ羽根の側端部 カゝら放つ液体原料を微粒子化させるカロ速度が側^ ¾に生じる速度で羽根を回転させ る。 この tb袓みによって円筒の内壁に沿って回転する粉体原料に微粒子ィ匕した液体 原料を回転軸の側から加える粉体原料に ¾~ "る液体原料の加え方。  5. The powder material is rotated along the inner wall of the cylinder! ^ The powder material is delivered to the powder material, and the end that discharges the liquid material rotates a blade whose acute angle is in the direction of the length of the rotation axis The speed of the caro-speed is provided on the shaft and the tip of the blade rotates the powder material along the inner wall of the cylinder, and the speed of the caro-speed to micronize the liquid material released from the side of the blade. Rotate the blades with. A method of adding the liquid raw material to the powdery raw material from the side of the rotation shaft, adding the fine particled liquid raw material to the powdery raw material rotating along the inner wall of the cylinder by this tb loading.
6. 粉体原料を円筒の内壁に沿って回転させる先端部が粉体原料に届き、 液体原料を放 つ側赚に液体原料を導く構造を持つ羽根を回転軸に設け、 羽根の先離 βに粉体原 料を内壁に沿って回転させるカロ速度が生じ、 カゝっ羽根の側 (5から放つ液体原料を 微粒子ィ匕させる加速度が側端部に生じる速度で羽根を回転させる。 この tb組みによ つて円筒の内壁に沿って回転する粉体原料に微粒子ィ匕した液体原料を回転軸の側か ら加える粉体原料に対する液体原料の加え方。  6. A blade with a structure that leads the powder material to the powder material and the tip to rotate the powder material along the inner wall of the cylinder reaches the powder material and guides the liquid material to the side weir is provided on the rotary shaft. In this case, the powder material is rotated along the inner wall, and the blade is rotated at such a speed that the acceleration causing the fine particles of the liquid material released from the side (5) is generated. How to add liquid material to powder material from the side of rotary shaft by adding fine particle liquid material to powder material rotating along inner wall of cylinder by assembling.
7. 粉体原科を円筒の内壁に沿って回転させる先端部が粉体原料に届き、 粉体原料に届 くことのない回転軸寄りの位置に液体原料を放つ他の先離を多段式に持つ羽根を 回転軸に設け、 粉体原料力 s接する先驗に粉体原料を円筒の内壁に沿って回転させ るカロ速度が生じ、 力 液体原料を放つ回転軸寄りの先端部に液体原料を微粒子化さ せるカロ速度が生じる; «で羽根を回転させる。 この ft祖みによつて円筒の内壁に沿 つて回転する粉体原料に微粒子化した液体原料を回転軸の側から加える粉体原料に 対する液体原料の力 Dえ方。 7. The tip that rotates the powder basics along the inner wall of the cylinder reaches the powder material, and discharges the liquid material to a position near the rotation axis that does not reach the powder material. The blade on the rotary shaft is provided on the rotary shaft, and the powder material is rotated along the inner wall of the cylinder at the tip of the powder material force contact. The speed of the carot is generated, and the speed of the carot which causes the liquid material to be micronized is generated at the tip near the rotation axis that releases the liquid material; The force of the liquid material on the powder material is added by adding the finely divided liquid material from the side of the rotating shaft to the powder material rotating along the inner wall of the cylinder by means of this ft cavitation.
8. 粉体原料を円筒の内壁に沿って回転させ、 液体原料を微粒子化する装置の一部ある レ、は全部を円筒の外部に置き、 生成された微粒子状の液体原料を円筒の内部に導き、 円筒の内壁に沿って回転する粉体原料に微粒子化した液体原料を回転軸の側から加 える粉体原料に対する液体原料の加え方。  8. The powder material is rotated along the inner wall of the cylinder, and there is a part of the device that atomizes the liquid material. Place the whole on the outside of the cylinder and make the generated particulate liquid material inside the cylinder. How to add the liquid material to the powder material by introducing and atomizing the liquid material finely divided into the powder material rotating along the inner wall of the cylinder from the rotary shaft side.
PCT/JP2003/008119 2003-04-16 2003-06-26 Method of mixing powder raw material and liquid raw material. WO2004091761A1 (en)

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 (en) 2004-10-28

Family

ID=33296756

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2003/008119 WO2004091761A1 (en) 2003-04-16 2003-06-26 Method of mixing powder raw material and liquid raw material.

Country Status (2)

Country Link
AU (1) AU2003304039A1 (en)
WO (1) WO2004091761A1 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103109884A (en) * 2012-12-02 2013-05-22 乐正午 Rotating pipe type dough making device
CN105854708A (en) * 2016-06-06 2016-08-17 无锡市翱宇特新科技发展有限公司 Efficient chemical raw material mixing device
CN106320150A (en) * 2016-10-21 2017-01-11 西安建筑科技大学 Steel slag asphalt permeable mixture double-shaft double-mixing device and mixing technology
CN106512826A (en) * 2016-12-04 2017-03-22 重庆市江津区驴溪酒厂有限责任公司 Stirring device used for liquor production
GB2569941A (en) * 2017-11-17 2019-07-10 Xaar 3D Ltd Apparatus for the manufacture of three-dimensional objects
CN111010970A (en) * 2019-12-31 2020-04-17 重庆酷熊科技有限公司 A fertilizer injection unit for liquid fertilizer
CN111034446A (en) * 2019-12-31 2020-04-21 重庆酷熊科技有限公司 Humic acid fertilizer fertilization equipment

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55119430A (en) * 1980-02-15 1980-09-13 Nisshin Flour Milling Co Ltd Mixing device of powder and granular material
JPS5640425A (en) * 1979-09-08 1981-04-16 Yasuro Ito Continuous mixing method and apparatus therefor
JPS57136925A (en) * 1981-02-18 1982-08-24 Hoshino Bussan Kk Continuous and homogeneous hydromixer
JPS58141726U (en) * 1982-03-19 1983-09-24 株式会社新明製作所 Molasses mixer equipment for solid feed
JPS63214328A (en) * 1987-09-25 1988-09-07 Kitagawa Tekkosho:Kk Horizontal multi-shaft type mixing device
JPS63251059A (en) * 1987-04-06 1988-10-18 Tooc Kogyo Kk Preparation of pasta and device therefor
US5372424A (en) * 1992-03-18 1994-12-13 Assistance Maintenance Industrielle Gildasienne Screw mixer, particulary for foundry molds
JP2001079827A (en) * 1999-09-10 2001-03-27 B M Syst:Kk In-pipeline mixing apparatus

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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 (en) * 1982-03-19 1983-09-24 株式会社新明製作所 Molasses mixer equipment for solid feed
JPS63251059A (en) * 1987-04-06 1988-10-18 Tooc Kogyo Kk Preparation of pasta and device therefor
JPS63214328A (en) * 1987-09-25 1988-09-07 Kitagawa Tekkosho:Kk Horizontal multi-shaft type mixing device
US5372424A (en) * 1992-03-18 1994-12-13 Assistance Maintenance Industrielle Gildasienne Screw mixer, particulary for foundry molds
JP2001079827A (en) * 1999-09-10 2001-03-27 B M Syst:Kk In-pipeline mixing apparatus

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103109884A (en) * 2012-12-02 2013-05-22 乐正午 Rotating pipe type dough making device
CN105854708A (en) * 2016-06-06 2016-08-17 无锡市翱宇特新科技发展有限公司 Efficient chemical raw material mixing device
CN106320150A (en) * 2016-10-21 2017-01-11 西安建筑科技大学 Steel slag asphalt permeable mixture double-shaft double-mixing device and mixing technology
CN106512826A (en) * 2016-12-04 2017-03-22 重庆市江津区驴溪酒厂有限责任公司 Stirring device used for liquor production
GB2569941A (en) * 2017-11-17 2019-07-10 Xaar 3D Ltd Apparatus for the manufacture of three-dimensional objects
CN111010970A (en) * 2019-12-31 2020-04-17 重庆酷熊科技有限公司 A fertilizer injection unit for liquid fertilizer
CN111034446A (en) * 2019-12-31 2020-04-21 重庆酷熊科技有限公司 Humic acid fertilizer fertilization equipment
CN111010970B (en) * 2019-12-31 2021-01-29 重庆酷熊科技有限公司 A fertilizer injection unit for liquid fertilizer

Also Published As

Publication number Publication date
AU2003304039A1 (en) 2004-11-04

Similar Documents

Publication Publication Date Title
US3502305A (en) Method of and apparatus for adding liquid to pulverulent or granular materials
US4511093A (en) Mixer-granulator drier
JPS607527B2 (en) Continuous homogenization or emulsification method of liquids and ultrasonic device for carrying out this method
US4499561A (en) Apparatus for continuously producing a dry material and liquid slurry
WO2004091761A1 (en) Method of mixing powder raw material and liquid raw material.
IE49492B1 (en) Treating calcined gypsum
US4478519A (en) Automatic paste-producing apparatus
JP2023515180A (en) Device for crushing beer lees and production line including it
JPS61187929A (en) Mixing and bonding device of powdery material
CN109127013B (en) Prevent sand mill of jam
CN207655053U (en) A kind of material-stirring device
US7717612B2 (en) Device for continuously mixing a food dough provided with two types of superimposed mixing tools and a side discharge
JP5061789B2 (en) Coating equipment
CN212119851U (en) Compound enzyme preparation configuration device
WO2006011266A1 (en) Method of combining powder material with liquid material and mixer
CN104642428B (en) A kind of continuous machine for steaming
CN208943996U (en) A kind of veterinary drug preparation mixing arrangement
CN207591711U (en) A kind of mixed and modified device of active carbonic acid gravity
JPS6411329B2 (en)
CN208066192U (en) Honey mixing apparatus
WO2008015756A1 (en) Apparatus for mixing powdery material with liquid material and method of producing mixture by using the mixing apparatus
US10736328B2 (en) Hydrator
CN107243267A (en) A kind of multi-functional full-automatic poultry feed agitating device
CN216171551U (en) Horizontal double helical ribbon blendor in no dead angle
CN214552841U (en) Automatic hybrid system of frequency conversion

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SC SD SE SG SK SL TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: JP

WWW Wipo information: withdrawn in national office

Country of ref document: JP

122 Ep: pct application non-entry in european phase