WO2014010062A1 - Degassing method and device for same - Google Patents

Degassing method and device for same Download PDF

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Publication number
WO2014010062A1
WO2014010062A1 PCT/JP2012/067836 JP2012067836W WO2014010062A1 WO 2014010062 A1 WO2014010062 A1 WO 2014010062A1 JP 2012067836 W JP2012067836 W JP 2012067836W WO 2014010062 A1 WO2014010062 A1 WO 2014010062A1
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bubble
pores
liquid
deaeration
bubbles
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PCT/JP2012/067836
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French (fr)
Japanese (ja)
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荒井孝一
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株式会社荒井鉄工所
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Priority to PCT/JP2012/067836 priority Critical patent/WO2014010062A1/en
Priority to JP2014524554A priority patent/JP6012730B2/en
Publication of WO2014010062A1 publication Critical patent/WO2014010062A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0036Flash degasification
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0042Degasification of liquids modifying the liquid flow
    • B01D19/0047Atomizing, spraying, trickling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0042Degasification of liquids modifying the liquid flow
    • B01D19/0052Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused

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  • a defoaming apparatus or method called a cyclone or a centrifugal separation system is known (see, for example, Patent Document 1 and Patent Document 2).
  • the present invention has been made paying attention to the above points, and is not simply a mesh or a filter body, but is provided with an element having pores and a bubble scratch that slides on the pore surface.
  • Pressure reduction that can change the decompression state in the decompression air intake means and the decompression vessel at the time of passage by enlarging and enlarging the gas when the foam-containing liquid passes through the pores by interposing the treatment process It is an object of the present invention to provide a novel defoaming method and apparatus capable of efficiently degassing with an adjustment tube configuration.
  • the present invention can solve the above problems by providing the following configuration.
  • a foam-containing liquid supply step of pressure-transferring the foam-containing liquid toward the wall surface having pores A bubble expanding step for collecting and expanding bubbles in the pores of the wall;
  • a defoaming method comprising a bubble scratching step of sliding on the wall surface before the bubble expansion step.
  • a foam-containing liquid supply mechanism for pressure-feeding the foam-containing liquid;
  • a deaeration / intake / exhaust treatment mechanism for sucking and exhausting bubbles in the decompression vessel;
  • a depressurization adjusting pipe mechanism capable of adjusting a depressurization state acting on a degassed liquid in a depressurization state of the degassing / exhaust treatment mechanism;
  • a liquid transfer mechanism for transferring defoamed liquid;
  • a defoaming apparatus comprising a bubble scratching mechanism for slidingly scratching the surface of the pores on the wall surface of the bubble expanding mechanism.
  • the bubble expansion mechanism has a cylindrical configuration having pores, and supplies the bubble-containing liquid to be supplied under pressure to either the inside or the outside of the cylindrical configuration and passes through the pores of the bubble expansion wall surface.
  • the defoaming device according to (2) above, wherein the defoaming device can be fed to the deaeration / intake / exhaust processing mechanism.
  • the bubble enlarging mechanism has a gap between adjacent long wires supported and fixed by a frame as pores, the width of the pores being from micron to millimeter, and bubbles in the liquid passing therethrough
  • the defoaming apparatus according to any one of (2) and (3), wherein the degassing apparatus is configured to increase the number by combining them together.
  • the bubble enlarging mechanism has pores that allow a bubble-containing liquid to pass between a grooved frame, a wire rod locked to the grooved frame, and an adjacent wire to bond and expand bubbles.
  • the pressure reducing adjustment pipe mechanism is open to the pressure reducing degassing side and the atmosphere opening side, and is configured to be able to adjust the opening degree of the control valve to introduce outside air on the atmosphere opening side. Defoaming device as described.
  • bubbles in various liquids cannot be degassed depending on the type of liquid and the size of the viscosity, but by passing through long pores, the bubbles in the liquid overlap and expand. It can pass through, and a trumpet-shaped enlarged part is formed on the discharge side while passing, so that the expansion of bubbles is promoted, the vaporization action is accelerated by the reduced pressure environment, and the bubbles in the liquid rapidly Vaporized and exhausted.
  • the deaeration expansion element has a cylindrical shape or a conical shape with an opening at the top, and can form foam-containing liquid in different types of inside-outside or outside-in, depending on the type of foam-containing liquid.
  • the scraper piece can be used to bring the surface of the pores into a scratching contact and push the bubbles into the pores or divide and cut large bubbles to promote the miniaturization of the bubbles and enter the pores. There are effects such as being able to be performed effectively.
  • the depressurization state of the degassing / exhaust treatment mechanism can be adjusted by the depressurization adjusting pipe mechanism, so that the unexcluded gas in the defoamed liquid that has not been discharged can be completely exhausted.
  • (d) shows the case where long holes that can be used for both types are used as pores.
  • (A) is a partially enlarged cross-sectional view showing the pore structure of a frame body in which a wire rod fitted to the deaeration expansion element shown in (a) and (b) of FIG. 5 is inserted
  • (b) is a diagram.
  • 5 is a partially enlarged cross-sectional view showing the pore structure of the deaeration expansion element shown in 5 (c) and (d) 5 (a) and 5 (b), the shape of the pores through which the foam-containing liquid formed is circulated is varied depending on the cross-sectional shape of the cross-sectional shape of the wire.
  • (A) is a wire with an equilateral triangular cross section
  • (b) is a wire with an isosceles triangular cross section
  • (c) is a wire with a cross-section base pentagon
  • (d ) Shows a case where a circular wire is used
  • (e) shows a case where an elliptical cross-section wire is used.
  • the deaeration expansion element 3 includes a spiral groove 5 on the outer periphery of a cylindrical frame 4, and the groove 5 shown in FIG. ), (B), (c), (d), and (e) have a cross-sectional shape such as a circle, a triangle, a pentagon, and an ellipse.
  • the gap between the adjacent wire rods 6 is defined as the pores 7 to serve as the pores for the foam-containing liquid. Then, as shown in FIG. 6A, the sharp side of the wire 6 can be engaged and fixed in the concave groove 5 to keep the width W of the pore 7 at a predetermined size, and the sharp side.
  • the scraper piece 12 has its sliding contact side slidably contacted with the outer periphery of the deaeration expansion element 3 at an acute or obtuse angle to promote the effect of pushing bubbles in the liquid into the pores 7. It is also possible to effectively remove the solid matter in the liquid by filtration.
  • FIG. 13 is a frame for supporting the scraper piece 12
  • 14 is a hollow rotating shaft for rotating the frame 13
  • 15 is a large gear provided at the end of the rotating shaft 14
  • 16 is the large gear 15
  • engages can be shown and it can drive by the motor 17.
  • FIG. Reference numeral 18 denotes a bearing disposed on the hollow rotating shaft 14.
  • a depressurization adjusting pipe mechanism 19 is provided in the deaeration / intake / exhaust processing mechanism 8. Specifically, one end of the tube body is opened to the atmosphere side, and the outside air is sucked in an adjustable manner, and the deaeration / exhaust process is performed. The depressurization state in the mechanism 8 can be freely adjusted in size, and the other end faces the deaeration / intake / exhaust processing mechanism 8.
  • Reference numeral 20 denotes an openable and closable adjustment valve provided in the pressure reducing adjustment pipe mechanism 19 which can adjust the introduction of the atmosphere freely.
  • a desired bubble-containing liquid produced or manufactured in advance is supplied to the bubble-containing liquid supply mechanism 1 using a pressurizing means such as a pump and supplied toward the bubble expansion mechanism 2 in the next stage.
  • the degassed liquid flows down along the inner peripheral surface of the deaeration expansion element 3 and is stored in a container below the deaeration intake / exhaust treatment mechanism 8 without foaming.
  • the required amount of air is inhaled, and the pressure in the container can be freely changed to maintain the water level of the defoamed liquid in a desired state.
  • the favorite liquid by which the deaeration process was carried out from the liquid transfer mechanism 10 of the next stage liquid can be obtained.
  • the outlet side of the pore 7 shown in FIG. 7 has a trumpet shape ⁇ in cross section, the bubbles in the foam-containing liquid tend to vaporize due to the action of decompression expansion during the discharge operation of the pore 7. Inspired, more effective vaporization can be performed.
  • the bubbles are effectively reduced by the sliding contact scratching action of the scraper piece 12 on the surface of the pores of the deaeration expansion element 3 with the bubbles and impurities during the production. Inside, the foreign matter is removed, and the back is lined up to homogenize the raw koji, contributing to quality improvement.
  • the bubbles that are pushed into the pores are united with each other and are effectively exhausted by the intake means immediately after passing.
  • the deaeration expansion element 3a of the bubble expansion mechanism 2 shown in FIGS. 3 and 4 is provided with a spiral groove 5 on the inner periphery of the frame body 4, and the wire 6 is engaged in the groove 5.
  • 1 and 2 has a flow mechanism that is formed from the inside to the outside, while the working mechanism of the pore 7 in FIGS. 1 and 2 is from outside to inside. This is the point where it circulates in and out, and everything else is the same constituent action.
  • the rotating shaft 14a is not hollow and has a normal shaft structure.
  • the scrapers 12 and 12a shown in FIGS. 1 and 2 and the scraper pieces 12 and 12a shown in FIGS. 3 and 4 increase the vertical width or swirl the entire foam-containing liquid as a spiral blade. In addition, it is possible to distribute the foam-containing liquid to the pores 7 effectively and at high speed.
  • the entire apparatus is shown in a vertical configuration in the vertical direction, but a configuration arrangement in an oblique direction can be similarly implemented.
  • deaeration expansion elements 3 and 3a are cylindrical, it is also possible to make it conical shape with the upper end portion cut off.
  • a flat plate with a plate thickness of 0.3 mm to 10 mm of a preferred metal or hard synthetic resin material is drilled with a large number of round holes or long holes 7 such as long holes by laser processing, and is bent into a cylindrical shape.
  • the manufacturing process such as processing with a drawn steel pipe, can be carried out by a desired method. And it can be provided as a straight cylindrical shape or a conical shape with the top and bottom cut off.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Degasification And Air Bubble Elimination (AREA)

Abstract

Provided are a novel degassing method and a device for the same that can deaerate efficiently by disposing an element provided with a large number of pores and providing a gas scraping processing mechanism that slides along a porous surface, and by having a reduced pressure adjustment tube constitution that can vary a reduced pressure state within a reduced pressure air suction means and a vacuum vessel by combining and expanding gases and expanding the size of bubbles when a liquid containing bubbles passes through the pores.

Description

脱泡方法及びその装置Defoaming method and apparatus
 本発明は、ミルク、豆乳、果汁などの各種食品、健康補助食品又は栄養剤、ドリンク剤等の医薬品或は、美顔液、洗髪料等の化粧品、更には塗料、バッテリーペースト、その他高分子樹脂等の粘性のある液状体を含む種々の液状体中に混在する気泡を機械的に排除する脱泡方法及びその装置に関する。 The present invention includes various foods such as milk, soy milk and fruit juice, health supplements or nutrients, pharmaceuticals such as drinks, cosmetics such as facial liquids and hair washing materials, paints, battery pastes, other polymer resins, etc. The present invention relates to a defoaming method and apparatus for mechanically eliminating bubbles mixed in various liquid materials including a viscous liquid material.
 液体状の各種食品、化成品、医薬品等の製造過程における気泡の混入は製品の容量の誤差、品質低下、劣化等の多くの弊害を伴い、最終工程を含み製造過程中に気体を除去する消気、脱気等の処理工程が組み込まれている。 The inclusion of bubbles in the production process of various liquid foods, chemical products, pharmaceuticals, etc. is accompanied by many adverse effects such as product volume error, quality degradation, and deterioration. Processing steps such as gas and deaeration are incorporated.
 上記液体製品の製造過程に混入ないし発生する気泡は、有効に排除するもので、数多くの構成、装置が知られている。 The air bubbles mixed or generated in the manufacturing process of the liquid product are effectively eliminated, and many configurations and devices are known.
 例えば、サイクロンないし遠心分離方式と呼ばれる脱泡装置や方法が知られている(例えば、特許文献1、特許文献2参照)。 For example, a defoaming apparatus or method called a cyclone or a centrifugal separation system is known (see, for example, Patent Document 1 and Patent Document 2).
特開2006-27012号公報JP 2006-27012 A 特開平10-43293号公報JP 10-43293 A
 上記した特許文献1,2は、いずれも含泡液体を容器内へ導入するに際し、円周方向に旋回させてその旋回流通路に塞板として網板を配設して気泡を分離させていたり、中央に設けた円筒状の濾過体を配設して気泡を分離させて液体分と分離させて脱泡しており、単に網の目や濾過体の目の大きさによって脱気分が規制されるという問題は避けられない。 In each of Patent Documents 1 and 2 described above, when introducing the foam-containing liquid into the container, the bubbles are separated by swirling in the circumferential direction and arranging a mesh plate as a closing plate in the swirling flow passage. In the center, a cylindrical filter body is arranged to separate bubbles and separate from the liquid to remove bubbles, and the deaeration is restricted simply by the mesh size and the size of the filter body. This problem is inevitable.
 本発明は、叙上の点に着目して成されたもので、単に網とか濾過体の目ではなく、細孔を備えたエレメントを配設すると共に、細孔面を摺動する気泡引掻処理工程を介装して、細孔での含泡液体の通過時に気体を合体,拡大させて気泡の大きさを拡大させて通過時の減圧吸気手段並びに減圧容器内の減圧状態を可変できる減圧調整管構成によって効率よく脱気できるようにした新規な脱泡方法及びその装置を提供することを目的とする。 The present invention has been made paying attention to the above points, and is not simply a mesh or a filter body, but is provided with an element having pores and a bubble scratch that slides on the pore surface. Pressure reduction that can change the decompression state in the decompression air intake means and the decompression vessel at the time of passage by enlarging and enlarging the gas when the foam-containing liquid passes through the pores by interposing the treatment process It is an object of the present invention to provide a novel defoaming method and apparatus capable of efficiently degassing with an adjustment tube configuration.
 この発明は下記の構成を備えることにより上記課題を解決できるものである。 The present invention can solve the above problems by providing the following configuration.
 (1)含泡液体を、細孔を有する壁面に向けて加圧移送させる含泡液体供給工程と、
 前記壁面の細孔内で気泡を集合拡大させる気泡拡大工程と、
 前記壁面の細孔を通過した含泡液体を減圧容器内で気泡を吸引排気する脱気吸排処理工程と、
 前記減圧容器内の減圧状態を調節自在に減圧する減圧管を備えた減圧調整管工程と、
 脱泡処理された液体を取り出す液体移送工程と、
より成り、前記気泡拡大工程の前段に壁面表面を摺動する気泡引掻処理工程を設けて成ることを特徴とする脱泡方法。
(1) a foam-containing liquid supply step of pressure-transferring the foam-containing liquid toward the wall surface having pores;
A bubble expanding step for collecting and expanding bubbles in the pores of the wall;
A deaeration / intake / exhaust treatment step of sucking and exhausting bubbles in the decompression vessel of the bubble-containing liquid that has passed through the pores of the wall surface;
A depressurization adjusting pipe step including a depressurization pipe for depressurizing the depressurization state in the depressurization container in an adjustable manner;
A liquid transfer step of taking out the defoamed liquid;
A defoaming method comprising a bubble scratching step of sliding on the wall surface before the bubble expansion step.
 (2)含泡液体を加圧送給する含泡液体供給機構と、
 細孔を穿った気泡拡大壁面を備えた気泡拡大機構と、
 含泡液体を減圧容器内で気泡を吸引排気する脱気吸排処理機構と、
 前記脱気吸排処理機構の減圧状態の脱泡液体に働く減圧状態を調節できる減圧調整管機構と、
 脱泡液体を移送する液体移送機構と、
より成り、前記気泡拡大機構の壁面には細孔の表面を摺動引掻する気泡引掻処理機構を介装して成ることを特徴とする脱泡装置。
(2) a foam-containing liquid supply mechanism for pressure-feeding the foam-containing liquid;
A bubble expansion mechanism with a bubble expansion wall with pores;
A deaeration / intake / exhaust treatment mechanism for sucking and exhausting bubbles in the decompression vessel;
A depressurization adjusting pipe mechanism capable of adjusting a depressurization state acting on a degassed liquid in a depressurization state of the degassing / exhaust treatment mechanism;
A liquid transfer mechanism for transferring defoamed liquid;
A defoaming apparatus comprising a bubble scratching mechanism for slidingly scratching the surface of the pores on the wall surface of the bubble expanding mechanism.
 (3)気泡拡大機構は、細孔を有する筒構成を備え、加圧送給される含泡液体を前記筒構成の内部又は外部のいずれか一方に送給し、気泡拡大壁面の細孔を通過させて脱気吸排処理機構に送給できるようにして成ることを特徴とする前記(2)記載の脱泡装置。 (3) The bubble expansion mechanism has a cylindrical configuration having pores, and supplies the bubble-containing liquid to be supplied under pressure to either the inside or the outside of the cylindrical configuration and passes through the pores of the bubble expansion wall surface. The defoaming device according to (2) above, wherein the defoaming device can be fed to the deaeration / intake / exhaust processing mechanism.
 (4)気泡拡大機構は、枠体で支持固定される長尺な線材の隣り合う間隔を細孔となし、該細孔の幅をミクロン単位からミリ単位の長さとし、通過する液体中の気泡を集合合体させて増大できるようにして成ることを特徴とする前記(2)又は(3)いずれか一項記載の脱泡装置。 (4) The bubble enlarging mechanism has a gap between adjacent long wires supported and fixed by a frame as pores, the width of the pores being from micron to millimeter, and bubbles in the liquid passing therethrough The defoaming apparatus according to any one of (2) and (3), wherein the degassing apparatus is configured to increase the number by combining them together.
 (5)気泡拡大機構は、溝付枠体と、この溝付枠体に係止される線材と、隣り合う線材との間に含泡液体を通過させて気泡を結合,拡大させる細孔を形成できる脱気拡大エレメントとして形成して成ることを特徴とする前記(2),(3)又は(4)いずれか一項記載の脱泡装置。 (5) The bubble enlarging mechanism has pores that allow a bubble-containing liquid to pass between a grooved frame, a wire rod locked to the grooved frame, and an adjacent wire to bond and expand bubbles. The defoaming device according to any one of (2), (3), and (4), wherein the defoaming device is formed as a deaeration expansion element that can be formed.
 (6)細孔を構成する隣り合う線材の間隔は排出側に向かって断面ラッパ状に形成して成ることを特徴とする前記(2)乃至(5)いずれか一項記載の脱泡装置。 (6) The defoaming device according to any one of (2) to (5), wherein an interval between adjacent wires constituting the pore is formed in a cross-sectional trumpet shape toward the discharge side.
 (7)気泡拡大機構は、板厚0.3mm~10mmの平面板にレーザ加工で多数の丸孔又は長孔などの細孔を穿ち筒状の脱気拡大エレメントに形成して、筒状の脱気拡大エレメントの内側から外側へ又は外側から内側へのいずれか一方へ通過する液体中の気泡を集合合体させて増大できるようにして成ることを特徴とする前記(2)記載の脱泡装置。 (7) The bubble expansion mechanism is formed by forming a cylindrical deaeration expansion element by drilling a large number of holes such as round holes or long holes by laser processing on a flat plate having a plate thickness of 0.3 mm to 10 mm. The defoaming device according to (2), wherein bubbles in the liquid passing through either the inner side to the outer side or the outer side to the inner side of the deaeration expansion element can be combined and increased. .
 (8)気泡拡大機構は、円筒形又は両端を開口した截円錐状のうちの一つ構成を備えたことを特徴とする前記(2)ないし(7)いずれか一項記載の脱泡装置。 (8) The defoaming device according to any one of (2) to (7), wherein the bubble expanding mechanism includes one of a cylindrical shape and a conical shape having both ends opened.
 (9)気泡拡大機構の脱気拡大エレメントは、スクレーパ片を設けて、細孔表面を引掻摺動できるようにして成ることを特徴とする前記(5)記載の脱泡装置。 (9) The deaeration device according to (5), wherein the deaeration expansion element of the bubble expansion mechanism is provided with a scraper piece so that the surface of the pores can be scratched and slid.
 (10)減圧調整管機構は、減圧脱泡側と大気開放側に開口し、大気開放側の外気の導入を調節弁の開口度を調節できるようにして成ることを特徴とする前記(2)記載の脱泡装置。 (10) The pressure reducing adjustment pipe mechanism is open to the pressure reducing degassing side and the atmosphere opening side, and is configured to be able to adjust the opening degree of the control valve to introduce outside air on the atmosphere opening side. Defoaming device as described.
 本発明によれば、各種液体中の気泡は、液体の種類や粘度の大きさによって、中々脱気できないが、長尺な細孔を通過させることにより、液体中の気泡は重なり重合拡大して通過できると共に、通過中の排出側にはラッパ状の拡大部分が形成されているので、気泡の拡大が促進され、減圧環境によって上方への気化作用が速まり、液中の気泡分は急速に気化排気される。 According to the present invention, bubbles in various liquids cannot be degassed depending on the type of liquid and the size of the viscosity, but by passing through long pores, the bubbles in the liquid overlap and expand. It can pass through, and a trumpet-shaped enlarged part is formed on the discharge side while passing, so that the expansion of bubbles is promoted, the vaporization action is accelerated by the reduced pressure environment, and the bubbles in the liquid rapidly Vaporized and exhausted.
 脱気拡大エレメントは円筒状、又は上部を開口した截円錐状等を呈し、含泡液体を内-外又は外-内の異なるタイプに形成でき、含泡液体の種類に応じていずれかのタイプのものを利用でき、更にスクレーパ片を設けることにより細孔表面を引掻摺接させて気泡の細孔への押入ないし大きな気泡の分割裁断により気泡の小型化を促して細孔への進入を有効に行わせることができるなどの効果を奏する。 The deaeration expansion element has a cylindrical shape or a conical shape with an opening at the top, and can form foam-containing liquid in different types of inside-outside or outside-in, depending on the type of foam-containing liquid. In addition, the scraper piece can be used to bring the surface of the pores into a scratching contact and push the bubbles into the pores or divide and cut large bubbles to promote the miniaturization of the bubbles and enter the pores. There are effects such as being able to be performed effectively.
 併せて脱気吸排処理機構の減圧状態を減圧調整管機構で調節できるので、未排出状態の脱泡液体中の未排除の気体も完全に排気できる。 At the same time, the depressurization state of the degassing / exhaust treatment mechanism can be adjusted by the depressurization adjusting pipe mechanism, so that the unexcluded gas in the defoamed liquid that has not been discharged can be completely exhausted.
本発明に係る脱泡装置の基本的構成である外-内タイプの一例を示す縦断説明図Longitudinal explanatory view showing an example of an outer-inner type which is a basic configuration of a defoaming apparatus according to the present invention 図1のII-II線断面図II-II sectional view of FIG. 本発明に係る脱泡装置の基本的構成である内-外タイプの一例を示す縦断説明図Longitudinal explanatory view showing an example of an inner-outer type which is a basic configuration of a defoaming apparatus according to the present invention 図3のIV-IV線断面図IV-IV sectional view of FIG. 本発明の脱泡装置に用いられる脱気拡大エレメントの4例を示す斜面図を示し、(a)は外-内タイプ、(b)は内-外タイプ、(c)は内-外又は外-内の両タイプに利用できる丸孔を細孔とした場合、(d)は内-外又は外-内の両タイプに利用できる長孔を細孔とした場合を示す4 is a perspective view showing four examples of deaeration expansion elements used in the defoaming device of the present invention, where (a) is an outer-inner type, (b) is an inner-outer type, and (c) is an inner-outer or outer side. -When round holes that can be used for both types are used as pores, (d) shows the case where long holes that can be used for both types are used as pores. (a)は図5の(a),(b)に示す脱気拡大エレメントに捲装される線材が係入される枠体の細孔構成を示す一部拡大断面図、(b)は図5の(c),(d)に示す脱気拡大エレメントの細孔構成を示す一部拡大断面図(A) is a partially enlarged cross-sectional view showing the pore structure of a frame body in which a wire rod fitted to the deaeration expansion element shown in (a) and (b) of FIG. 5 is inserted, and (b) is a diagram. 5 is a partially enlarged cross-sectional view showing the pore structure of the deaeration expansion element shown in 5 (c) and (d) 図5(a),(b)に示す脱気拡大エレメントに形成される含泡液体を流通させる細孔の構造を線材の構造を線材の断面形状の断面形状の相違によって種々異なる形状が形成されるもので、(a)は断面正三角形の線材を用いた場合、(b)は断面二等辺三角形の線材を用いた場合、(c)は断面ベース型五角形の線材を用いた場合、(d)は円形の線材を用いた場合、(e)は断面楕円形の線材を用いた場合を示す5 (a) and 5 (b), the shape of the pores through which the foam-containing liquid formed is circulated is varied depending on the cross-sectional shape of the cross-sectional shape of the wire. (A) is a wire with an equilateral triangular cross section, (b) is a wire with an isosceles triangular cross section, (c) is a wire with a cross-section base pentagon, (d ) Shows a case where a circular wire is used, and (e) shows a case where an elliptical cross-section wire is used.
 以下に、本発明の実施例を説明する。 Hereinafter, examples of the present invention will be described.
 図1及び図2に本発明の代表的な外-内タイプの脱泡装置の一実施例を示す。 1 and 2 show an embodiment of a typical outer-inner type defoaming apparatus of the present invention.
 1は、含泡液体をポンプ等で加圧供給できる含泡液体供給機構を示し、加圧ポンプ等で好みの供給圧を以って含泡液体を供給できる。 1 shows a foam-containing liquid supply mechanism that can supply foam-containing liquid under pressure with a pump or the like, and the foam-containing liquid can be supplied with a desired supply pressure with a pressure pump or the like.
 2は、前記含泡液体供給機構1の後段に接続される気泡拡大機構を示し、筒状の脱気拡大エレメント3を備える。 2 indicates a bubble expansion mechanism connected to the subsequent stage of the bubble-containing liquid supply mechanism 1 and includes a cylindrical deaeration expansion element 3.
 この脱気拡大エレメント3は、図5(a),(b)に示すように、円筒状の枠体4の外周にスパイラル状の凹溝5を備え、この凹溝5内に図7(a),(b),(c),(d),(e)に示すような断面形状が円形,三角形,五角形,楕円形など、好みの形状を有する線材6を係合してスパイラル状に捲装し、隣り合う線材6同士の間隙を細孔7として含泡液体の流通孔とするものである。そして、図6(a)に示すように線材6の尖鋭側を凹溝5内に係入固定して細孔7の幅Wを予め設定された大きさに保持させることができると共に、尖鋭側を有しない断面円形,楕円形などの場合は、いずれか一方の側を凹溝5内に係入させて固定できる。これにより、捲装された線材6の非掛止側の壁面が平坦な構成のものは、図7の(a),(b)及び(c)であり、円弧凹凸状のものは図7の(d)及び(e)である。 As shown in FIGS. 5A and 5B, the deaeration expansion element 3 includes a spiral groove 5 on the outer periphery of a cylindrical frame 4, and the groove 5 shown in FIG. ), (B), (c), (d), and (e) have a cross-sectional shape such as a circle, a triangle, a pentagon, and an ellipse. The gap between the adjacent wire rods 6 is defined as the pores 7 to serve as the pores for the foam-containing liquid. Then, as shown in FIG. 6A, the sharp side of the wire 6 can be engaged and fixed in the concave groove 5 to keep the width W of the pore 7 at a predetermined size, and the sharp side. In the case of a circular cross section, an elliptical shape, or the like that does not have any, it can be fixed by engaging one of the sides into the groove 5. Thereby, the thing of the structure where the wall surface of the non-hanging side of the wire rod 6 is flat is (a), (b) and (c) of FIG. (D) and (e).
 この脱気拡大エレメント3は、外周に捲装された線材6を前記含泡液体供給機構1に臨ませ、含泡液体は細孔7を介して脱気拡大エレメント3の外周より内周に向けて図2の矢符方向に押入させて外-内タイプとして使用することができる。 In this deaeration expansion element 3, the wire 6 mounted on the outer periphery faces the bubble-containing liquid supply mechanism 1, and the bubble-containing liquid is directed from the outer periphery to the inner periphery via the pores 7. And can be used as an outside-inside type by pushing it in the direction of the arrow in FIG.
 8は、前記気泡拡大機構2の脱気拡大エレメント3の内筒側に形成される脱気吸排処理機構であって、上部には減圧機能を有する減圧ポンプ9を配設すると共に、脱気拡大エレメント3の下側には脱気されて容器内に滞溜させた液体を移送する液体移送機構10を接続してある。 Reference numeral 8 denotes a deaeration intake / exhaust processing mechanism formed on the inner cylinder side of the deaeration expansion element 3 of the bubble expansion mechanism 2, and a depressurization pump 9 having a depressurization function is disposed on the upper side, and the deaeration expansion A liquid transfer mechanism 10 is connected to the lower side of the element 3 to transfer the liquid that has been deaerated and accumulated in the container.
 11は、前記含泡液体供給機構1の後段に設けられる、気泡拡大機構2の脱気拡大エレメント3の外周を摺動する気泡引掻処理機構であって、具体的にはスクレーパ片12を備え、円筒状の脱気拡大エレメント3の外周面を回転して細孔7の周面に臨まれる液体中の気泡を細孔7に押入させたり、液体中の大きな気泡を細分化して細孔7への押入を効率的に行わせることができるように働く。なお、図示では直状形状であるが、円弧状ないしスパイラル状など好みの形状と長さで屈曲させて形成することもできる。なお、スクレーパ片12は、その摺接辺側を脱気拡大エレメント3の外周に対し、摺接角度を鋭角ないし鈍角に摺接させて液体中の気泡の細孔7への押入効果を促進したり、液体中の固形物の濾過排除を有効に行わせることも可能である。 Reference numeral 11 denotes a bubble scratching mechanism that slides on the outer periphery of the deaeration expansion element 3 of the bubble expansion mechanism 2 and is provided at the subsequent stage of the bubble-containing liquid supply mechanism 1, and specifically includes a scraper piece 12. Then, the outer peripheral surface of the cylindrical deaeration expansion element 3 is rotated so that the bubbles in the liquid facing the peripheral surface of the pores 7 are pushed into the pores 7, or the large bubbles in the liquid are subdivided into the pores 7 It works so that the intrusion into can be done efficiently. In addition, although it is a straight shape in the drawing, it can be formed by bending a desired shape and length such as an arc shape or a spiral shape. In addition, the scraper piece 12 has its sliding contact side slidably contacted with the outer periphery of the deaeration expansion element 3 at an acute or obtuse angle to promote the effect of pushing bubbles in the liquid into the pores 7. It is also possible to effectively remove the solid matter in the liquid by filtration.
 13は、前記スクレーパ片12を支持する枠、14はこの枠13を回転させるための中空状の回転軸、15はこの回転軸14の端部に設けた大歯車、16は前記大歯車15と噛合する小歯車を示し、モータ17により駆動させることができる。18は、中空状の回転軸14に配設されるベアリングを示す。 13 is a frame for supporting the scraper piece 12, 14 is a hollow rotating shaft for rotating the frame 13, 15 is a large gear provided at the end of the rotating shaft 14, and 16 is the large gear 15 The small gear which meshes | engages can be shown and it can drive by the motor 17. FIG. Reference numeral 18 denotes a bearing disposed on the hollow rotating shaft 14.
 19は前記脱気吸排処理機構8に配設される減圧調整管機構であって、具体的には管体の一端を大気側に開口し、外気を調節自在に吸引させて、脱気吸排処理機構8内の減圧状況を大小自由に調節でき、他端を脱気吸排処理機構8内に臨ませて置くものである。20は大気の導入を大小自在に調節できる前記減圧調整管機構19に設けられる開閉自在の調節弁である。 A depressurization adjusting pipe mechanism 19 is provided in the deaeration / intake / exhaust processing mechanism 8. Specifically, one end of the tube body is opened to the atmosphere side, and the outside air is sucked in an adjustable manner, and the deaeration / exhaust process is performed. The depressurization state in the mechanism 8 can be freely adjusted in size, and the other end faces the deaeration / intake / exhaust processing mechanism 8. Reference numeral 20 denotes an openable and closable adjustment valve provided in the pressure reducing adjustment pipe mechanism 19 which can adjust the introduction of the atmosphere freely.
 叙上の構成に基づいて作用を説明する。 The operation will be explained based on the above structure.
 予め製出、或は製造過程中の所望の含泡液体を、ポンプ等の加圧手段を用いて含泡液体供給機構1に供給し、次段の気泡拡大機構2に向けて供給する。 A desired bubble-containing liquid produced or manufactured in advance is supplied to the bubble-containing liquid supply mechanism 1 using a pressurizing means such as a pump and supplied toward the bubble expansion mechanism 2 in the next stage.
 この気泡拡大機構2の脱気拡大エレメント3には、その外周にスクレーパ片12を配設し、モータ17により回転作用が与えられているので、脱気拡大エレメント3の外周面、即ち細孔7の開口側はスクレーパ片12によって摺動され、従って、液体中の気泡は液体と共に細孔7内に強制的に押入されると共に、スクレーパ片12の回転作用により、細孔7を通過し難い液体中の大きな気泡は、截断されて小形化され同様に細孔7に押入される。 Since the scraper piece 12 is disposed on the outer periphery of the deaeration expansion element 3 of the bubble expansion mechanism 2 and is rotated by the motor 17, the outer peripheral surface of the deaeration expansion element 3, that is, the pore 7. Therefore, the bubbles in the liquid are forcibly pushed into the pores 7 together with the liquid, and the liquid that hardly passes through the pores 7 due to the rotating action of the scraper pieces 12. Large bubbles in the inside are cut and reduced in size and are similarly pushed into the pores 7.
 そして、細孔7内に押入された気泡は、隣り合う他の気泡と合体し、細孔7の流通中に拡大し、脱気吸排処理機構8内に入るや否や液体と遊離して上方に気化して脱気拡大エレメント3の内周面より速やかに脱気処理される。 The bubbles pushed into the pores 7 merge with other neighboring bubbles, expand during the circulation of the pores 7, and are released from the liquid as soon as they enter the deaeration / exhaust treatment mechanism 8. Vaporization is performed and the deaeration process is promptly performed from the inner peripheral surface of the deaeration expansion element 3.
 脱気された液体は、脱気拡大エレメント3の内周面に沿って流下し、泡立てることなく脱気吸排処理機構8の下部の容器内に貯溜されるが、減圧調整管機構19によって大気中の空気が必要量吸入され、容器内の圧力を自在に変更して脱泡液体の水位を好みの状態に保持できる。そして、次段の液体の液体移送機構10より脱気処理された好みの液体を得ることができる。 The degassed liquid flows down along the inner peripheral surface of the deaeration expansion element 3 and is stored in a container below the deaeration intake / exhaust treatment mechanism 8 without foaming. The required amount of air is inhaled, and the pressure in the container can be freely changed to maintain the water level of the defoamed liquid in a desired state. And the favorite liquid by which the deaeration process was carried out from the liquid transfer mechanism 10 of the next stage liquid can be obtained.
 ところで、細孔7は図7に示すように種々の構造を得ることができる。細孔7の幅Wに関しては、枠体4に凹設されたスパイラル状の凹溝5の隣り合う間隔によって好みの大きさのミクロン単位の大きさとすることができるが、奥行きVの長さは、断面形状で(d)の円形、又は(a),(b)の正三角形や二等辺三角形では極めて短いが、(c)の五角形、(e)の楕円形などの形状であっては比較的長尺になり、隣り合う気泡の合体拡大効果を促進することができる。 Incidentally, the pores 7 can have various structures as shown in FIG. With respect to the width W of the pore 7, it can be set to a desired micron unit size depending on the interval between adjacent spiral grooves 5 formed in the frame body 4. The cross-sectional shape of (d) circle, or (a), (b) equilateral triangle or isosceles triangle is very short, but (c) pentagon, (e) ellipse, etc. are compared. It is possible to promote the combined expansion effect of adjacent bubbles.
 更に、スクレーパ片12は、摺接する側の細孔7の開口面が図7の(a),(b)及び(c)の場合は、平坦状であるので、板状体で差支えないが、同図(d)及び(e)の場合は円弧の凹凸状であるので順応性のある刷毛状の方が好ましい。 Further, the scraper piece 12 is flat when the opening surface of the pore 7 on the sliding contact side is (a), (b) and (c) in FIG. In the case of (d) and (e) in the figure, the shape of the arc is uneven, and therefore a conformable brush shape is preferable.
 また、図7で示す細孔7の出口側は、断面ラッパ状αの形状を備えているので、含泡液体中の気泡は細孔7の排出操作時に減圧膨張の作用を受けて気化傾向が促されて、より有効な気化作用を行うことができる。 In addition, since the outlet side of the pore 7 shown in FIG. 7 has a trumpet shape α in cross section, the bubbles in the foam-containing liquid tend to vaporize due to the action of decompression expansion during the discharge operation of the pore 7. Inspired, more effective vaporization can be performed.
 具体的には、比較的粘性の高い豆腐製造時において、製造時の気泡と夾雑物とを脱気拡大エレメント3の細孔表面でスクレーパ片12の摺接引掻作用によって気泡は有効に細孔内に入り、夾雑物は取り除かれ、裏ごしされて生呉の均質化が図られ、品質向上に寄与する。細孔内に押入された気泡は、隣り合う同士が合一合体して、通過直後の吸気手段により有効に排気される。 Specifically, during the production of tofu with relatively high viscosity, the bubbles are effectively reduced by the sliding contact scratching action of the scraper piece 12 on the surface of the pores of the deaeration expansion element 3 with the bubbles and impurities during the production. Inside, the foreign matter is removed, and the back is lined up to homogenize the raw koji, contributing to quality improvement. The bubbles that are pushed into the pores are united with each other and are effectively exhausted by the intake means immediately after passing.
 即ち、一種の裏ごし脱泡となり、原料から夾雑物を除去し、粒子状及び繊維状の固形物や液体を均質分散し、滑らかにしながら脱泡し、原料の小泡化と均質化が得られる。 That is, it becomes a kind of defoaming on the back, removes impurities from the raw material, uniformly disperses particulate and fibrous solids and liquids, and defoams while smoothing to obtain a small foam and homogenization of the raw material .
 なお、図において、符号21は、気泡拡大機構2に入る前の細孔7の表面でスクレーパ片12で除去された固形分などを収容する裏ごし貯溜部、22はエアベント、23は枠体4を構成する孔を示す。 In the figure, reference numeral 21 denotes a back storage part for storing solids removed by the scraper pieces 12 on the surface of the pores 7 before entering the bubble expanding mechanism 2, 22 is an air vent, and 23 is the frame 4. The hole which comprises is shown.
 次に、図3及び図4において、本発明に係る他の代表的な内-外タイプの脱泡装置の実施例を示す。 Next, FIGS. 3 and 4 show another typical embodiment of the defoaming device of the inner-outer type according to the present invention.
 なお、図1及び図2と同一の構成については同一の符号を符し、説明の詳細は省く。 In addition, the same code | symbol is attached | subjected about the structure same as FIG.1 and FIG.2, and the detail of description is abbreviate | omitted.
 基本的に含泡液体供給機構1、気泡拡大機構2、脱気吸排気処理機構8、液体移送機構10及び減圧調整管機構19は図1及び図2と同一である。 Basically, the bubble-containing liquid supply mechanism 1, the bubble expansion mechanism 2, the deaeration / intake / exhaust treatment mechanism 8, the liquid transfer mechanism 10 and the decompression adjustment pipe mechanism 19 are the same as those in FIGS.
 両者の相違点は、図3及び図4に示す気泡拡大機構2の脱気拡大エレメント3aが枠体4の内周にスパイラル状の凹溝5を設け、この凹溝5内に線材6を係合させて隣り合う線材6間に細孔7を形成して、内から外へ向う流通機構を有しているのに対し、図1及び図2の細孔7の作用機構が外-内から内-外へ流通している点であり、それ以外はすべて同一の構成作用である。また、回転軸14aは中空状でなく通常の軸構造を示している。 The difference between the two is that the deaeration expansion element 3a of the bubble expansion mechanism 2 shown in FIGS. 3 and 4 is provided with a spiral groove 5 on the inner periphery of the frame body 4, and the wire 6 is engaged in the groove 5. 1 and 2 has a flow mechanism that is formed from the inside to the outside, while the working mechanism of the pore 7 in FIGS. 1 and 2 is from outside to inside. This is the point where it circulates in and out, and everything else is the same constituent action. Moreover, the rotating shaft 14a is not hollow and has a normal shaft structure.
 次に、スクレーパ片12aは、脱気拡大エレメント3aの内周面を摺動しているので、このスクレーパ片12aを支持回転する枠13aは、脱気拡大エレメント3aの中心軸上に設けた回転軸14aの上下に一対に設けて、スクレーパ片12aの上下を固定させてある。スクレーパ片12aの形状,構成は図1及び図2と同一であって異なる処はない。 Next, since the scraper piece 12a slides on the inner peripheral surface of the deaeration expansion element 3a, the frame 13a for supporting and rotating the scraper piece 12a is a rotation provided on the central axis of the deaeration expansion element 3a. A pair of upper and lower shafts 14a are provided to fix the upper and lower sides of the scraper piece 12a. The shape and configuration of the scraper piece 12a are the same as in FIGS. 1 and 2, and there is no difference.
 なお、図示しないが図1,図2の構成と図3,図4のスクレーパ片12,12aは上下方向の幅員を大きくしたり、捻回したスパイラル羽根状として含泡液体全体を旋回流動させて、細孔7への含泡液体を有効かつ高速に流通させることもできる。 Although not shown, the scrapers 12 and 12a shown in FIGS. 1 and 2 and the scraper pieces 12 and 12a shown in FIGS. 3 and 4 increase the vertical width or swirl the entire foam-containing liquid as a spiral blade. In addition, it is possible to distribute the foam-containing liquid to the pores 7 effectively and at high speed.
 更に、図示では装置全体が上下方向の縦型構成で示されているが、斜め方向での構成配置も同様に実施できる。 Furthermore, in the drawing, the entire apparatus is shown in a vertical configuration in the vertical direction, but a configuration arrangement in an oblique direction can be similarly implemented.
 また、脱気拡大エレメント3,3aは円筒状であるが、上端部分を切截した円錐状とすることも可能である。 Moreover, although the deaeration expansion elements 3 and 3a are cylindrical, it is also possible to make it conical shape with the upper end portion cut off.
 上記実施例において、脱気拡大エレメント3,3aはいずれも枠体4に種々断面構造の異なる線材6を用いて、筒状の枠体4の外周又は内周に捲装して線材6間の間隙を細孔7として含泡液体を通過させて、液体中の気泡を分離拡大させて脱気吸排処理機構8内で気泡を有効に分離排気させるようにしたものであるが、之等の構成に代え、図5(c),(d)に示す実施例では脱気拡大エレメント3b及び3cは、単に筒構成に多数の小孔とか長孔を穿ち、これらを孔の細孔7として含泡液体中の気泡を分離吸引させており、それ以外の構成はすべて前記実施例と同一であって、異なる処はない。 In the above embodiment, each of the deaeration expansion elements 3 and 3a uses the wire 6 having various cross-sectional structures for the frame body 4, and is fitted on the outer periphery or the inner periphery of the cylindrical frame body 4 between the wire members 6. The gap is made to pass through the bubble-containing liquid, and the bubbles in the liquid are separated and expanded so that the bubbles are effectively separated and exhausted in the deaeration / exhaust treatment mechanism 8. Instead, in the embodiment shown in FIGS. 5 (c) and 5 (d), the deaeration expansion elements 3b and 3c are simply formed with a plurality of small holes or long holes in the cylindrical structure, and these are included as pores 7 of the holes. Air bubbles in the liquid are separated and sucked, and all other configurations are the same as in the above embodiment, and there is no difference.
 具体的には好みの金属ないしは硬質合成樹脂材料の板厚0.3mm~10mmの平面板にレーザ加工で多数の丸孔ないし、長孔などの細孔7を穿ち、円筒状に曲折加工を施して形成するのが一般的であるが、引抜き鋼管による加工製作など、その製作加工は好みの方法で差支えない。そして、直状の円筒状ないし上下を切截した円錐状として提供できる。 Specifically, a flat plate with a plate thickness of 0.3 mm to 10 mm of a preferred metal or hard synthetic resin material is drilled with a large number of round holes or long holes 7 such as long holes by laser processing, and is bent into a cylindrical shape. In general, however, the manufacturing process, such as processing with a drawn steel pipe, can be carried out by a desired method. And it can be provided as a straight cylindrical shape or a conical shape with the top and bottom cut off.
 この種の脱泡方法及び脱泡装置は、ジュースなどの飲料,醤油,ソースなどの食品調味料,薬液などの食品用としては勿論のこと、化学薬品などの液体製品、その他化粧材料液体製品などの広範な液状製品の脱泡処理作業に広く実施できる。 This type of defoaming method and defoaming apparatus is used for beverages such as juice, food seasonings such as soy sauce and sauce, liquid products such as chemicals, liquid products such as chemicals, and other cosmetic material liquid products. It can be widely applied to the defoaming treatment of a wide range of liquid products.
 1   含泡液体供給機構
 2   気泡拡大機構
 3,3a,3b,3c  脱気拡大エレメント
 4   枠体
 5   凹溝
 6   線材
 7   細孔
 8   脱気吸排処理機構
 9   減圧ポンプ
 10  液体移送機構
 11  気泡引掻処理機構
 12,12a スクレーパ片
 13,13a 枠
 14,14a 回転軸
 15  大歯車
 16  小歯車
 17  モータ
 18  ベアリング
 19  減圧調整管機構
 20  調節弁
 21  裏ごし貯溜部
 22  エアベント
 23  孔
 W   細孔7の幅
 V   奥行き
 α   断面ラッパ状
DESCRIPTION OF SYMBOLS 1 Foam-containing liquid supply mechanism 2 Bubble expansion mechanism 3, 3a, 3b, 3c Deaeration expansion element 4 Frame body 5 Concave groove 6 Wire material 7 Pore 8 Deaeration intake / exhaust treatment mechanism 9 Pressure reduction pump 10 Liquid transfer mechanism 11 Bubble scratching process Mechanism 12, 12a Scraper piece 13, 13a Frame 14, 14a Rotating shaft 15 Large gear 16 Small gear 17 Motor 18 Bearing 19 Depressurization adjusting pipe mechanism 20 Control valve 21 Back storage part 22 Air vent 23 Hole W Hole 7 width V Depth α Cross-sectional trumpet shape

Claims (10)

  1.  含泡液体を、細孔を有する壁面に向けて加圧移送させる含泡液体供給工程と、
     前記壁面の細孔内で気泡を集合拡大させる気泡拡大工程と、
     前記壁面の細孔を通過した含泡液体を減圧容器内で気泡を吸引排気する脱気吸排処理工程と、
     前記減圧容器内の減圧状態を調節自在に減圧する減圧管を備えた減圧調整管工程と、
     脱泡処理された液体を取り出す液体移送工程と、
    より成り、前記気泡拡大工程の前段に壁面表面を摺動する気泡引掻処理工程を設けて成ることを特徴とする脱泡方法。
    A foam-containing liquid supply step of pressure-transferring the foam-containing liquid toward the wall surface having pores;
    A bubble expanding step for collecting and expanding bubbles in the pores of the wall;
    A deaeration / intake / exhaust treatment step of sucking and exhausting bubbles in the decompression vessel of the bubble-containing liquid that has passed through the pores of the wall surface;
    A depressurization adjusting pipe step including a depressurization pipe for depressurizing the depressurization state in the depressurization container in an adjustable manner;
    A liquid transfer step of taking out the defoamed liquid;
    A defoaming method comprising a bubble scratching step of sliding on the wall surface before the bubble expansion step.
  2.  含泡液体を加圧送給する含泡液体供給機構と、
     細孔を穿った気泡拡大壁面を備えた気泡拡大機構と、
     含泡液体を減圧容器内で気泡を吸引排気する脱気吸排処理機構と、
     前記脱気吸排処理機構の減圧状態の脱泡液体に働く減圧状態を調節できる減圧調整管機構と、
     脱泡液体を移送する液体移送機構と、
    より成り、前記気泡拡大機構の壁面には細孔の表面を摺動引掻する気泡引掻処理機構を介装して成ることを特徴とする脱泡装置。
    A foam-containing liquid supply mechanism for pressure-feeding the foam-containing liquid;
    A bubble expansion mechanism with a bubble expansion wall with pores;
    A deaeration / intake / exhaust treatment mechanism for sucking and exhausting bubbles in the decompression vessel;
    A depressurization adjusting pipe mechanism capable of adjusting a depressurization state acting on a degassed liquid in a depressurization state of the degassing / exhaust treatment mechanism;
    A liquid transfer mechanism for transferring defoamed liquid;
    A defoaming apparatus comprising a bubble scratching mechanism for slidingly scratching the surface of the pores on the wall surface of the bubble expanding mechanism.
  3.  気泡拡大機構は、細孔を有する筒構成を備え、加圧送給される含泡液体を前記筒構成の内部又は外部のいずれか一方に送給し、気泡拡大壁面の細孔を通過させて脱気吸排処理機構に送給できるようにして成ることを特徴とする請求項2記載の脱泡装置。 The bubble expanding mechanism has a cylindrical structure having pores, and supplies the bubble-containing liquid to be supplied under pressure to either the inside or the outside of the cylindrical structure, and passes through the pores on the bubble expanding wall surface to remove it. 3. A defoaming device according to claim 2, wherein the defoaming device is configured to be fed to an air intake / exhaust processing mechanism.
  4.  気泡拡大機構は、枠体で支持固定される長尺な線材の隣り合う間隔を細孔となし、該細孔の幅をミクロン単位からミリ単位の長さとし、通過する液体中の気泡を集合合体させて増大できるようにして成ることを特徴とする請求項2又は3いずれか一項記載の脱泡装置。 The bubble expansion mechanism has a gap between adjacent long wires supported and fixed by a frame as pores, the width of the pores is from micron to millimeter, and the bubbles in the passing liquid are aggregated together. The defoaming device according to claim 2, wherein the defoaming device is configured to be able to be increased.
  5.  気泡拡大機構は、溝付枠体と、この溝付枠体に係止される線材と、隣り合う線材との間に含泡液体を通過させて気泡を結合,拡大させる細孔を形成できる脱気拡大エレメントとして形成して成ることを特徴とする請求項2,3又は4いずれか一項記載の脱泡装置。 The bubble expansion mechanism is a detachment mechanism that can form pores that allow a bubble-containing liquid to pass between a grooved frame, a wire locked to the grooved frame, and an adjacent wire to bond and expand bubbles. The defoaming device according to any one of claims 2, 3 and 4, wherein the defoaming device is formed as a gas expansion element.
  6.  細孔を構成する隣り合う線材の間隔は排出側に向かって断面ラッパ状に形成して成ることを特徴とする請求項2乃至5いずれか一項記載の脱泡装置。 The defoaming device according to any one of claims 2 to 5, wherein an interval between adjacent wires constituting the pores is formed in a cross-sectional trumpet shape toward the discharge side.
  7.  気泡拡大機構は、板厚0.3mm~10mmの平面板にレーザ加工で多数の丸孔又は長孔などの細孔を穿ち筒状の脱気拡大エレメントに形成して、筒状の脱気拡大エレメントの内側から外側へ又は外側から内側へのいずれか一方へ通過する液体中の気泡を集合合体させて増大できるようにして成ることを特徴とする請求項2記載の脱泡装置。 The bubble expansion mechanism is a cylindrical deaeration expansion element that is formed in a cylindrical deaeration expansion element by drilling a large number of holes such as round holes or long holes by laser processing on a flat plate with a plate thickness of 0.3 mm to 10 mm. 3. The defoaming apparatus according to claim 2, wherein bubbles in the liquid passing from the inside to the outside of the element or from the outside to the inside of the element can be combined and increased.
  8.  気泡拡大機構は、円筒形又は両端を開口した截円錐状のうちの一つ構成を備えたことを特徴とする請求項2ないし7いずれか一項記載の脱泡装置。 The defoaming device according to any one of claims 2 to 7, wherein the bubble expanding mechanism has one configuration of a cylindrical shape or a conical shape having both ends opened.
  9.  気泡拡大機構の脱気拡大エレメントは、スクレーパ片を設けて、細孔表面を引掻摺動できるようにして成ることを特徴とする請求項5記載の脱泡装置。 6. The deaeration device according to claim 5, wherein the deaeration expansion element of the bubble expansion mechanism is provided with a scraper piece so that the surface of the pores can be scratched and slid.
  10.  減圧調整管機構は、減圧脱泡側と大気開放側に開口し、大気開放側の外気の導入を調節弁の開口度を調節できるようにして成ることを特徴とする請求項2記載の脱泡装置。 3. The defoaming apparatus according to claim 2, wherein the depressurization adjusting pipe mechanism opens to the depressurization defoaming side and the atmosphere opening side so that the opening degree of the control valve can be adjusted by introducing outside air on the atmosphere opening side. apparatus.
PCT/JP2012/067836 2012-07-12 2012-07-12 Degassing method and device for same WO2014010062A1 (en)

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Publication number Priority date Publication date Assignee Title
WO2015140904A1 (en) * 2014-03-17 2015-09-24 株式会社荒井鉄工所 Apparatus and method for slit nozzle spray defoaming
CN112791451A (en) * 2021-01-19 2021-05-14 绵阳世诺科技有限公司 Vacuum brushing type continuous defoaming machine
CN113117569A (en) * 2021-04-23 2021-07-16 深圳市红叶杰科技有限公司 Waste gas recovery device is used in production of two-component organosilicon casting glue
EP3954450A4 (en) * 2019-04-09 2023-02-22 M. Technique Co., Ltd. Vacuum degassing machine
EP3957392A4 (en) * 2019-04-15 2023-06-21 M. Technique Co., Ltd. Agitator

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JPS58202005A (en) * 1982-05-19 1983-11-25 Toyo Filter Kogyo Kk Apparatus for defoaming high viscosity concentrated liquid
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WO2015140904A1 (en) * 2014-03-17 2015-09-24 株式会社荒井鉄工所 Apparatus and method for slit nozzle spray defoaming
EP3954450A4 (en) * 2019-04-09 2023-02-22 M. Technique Co., Ltd. Vacuum degassing machine
EP3957392A4 (en) * 2019-04-15 2023-06-21 M. Technique Co., Ltd. Agitator
EP3957390A4 (en) * 2019-04-15 2023-06-21 M Technique Co., Ltd. Agitator
CN112791451A (en) * 2021-01-19 2021-05-14 绵阳世诺科技有限公司 Vacuum brushing type continuous defoaming machine
CN113117569A (en) * 2021-04-23 2021-07-16 深圳市红叶杰科技有限公司 Waste gas recovery device is used in production of two-component organosilicon casting glue

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