WO2014125612A1 - Deaeration method for bubble-containing liquid and device therefor - Google Patents

Deaeration method for bubble-containing liquid and device therefor Download PDF

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Publication number
WO2014125612A1
WO2014125612A1 PCT/JP2013/053693 JP2013053693W WO2014125612A1 WO 2014125612 A1 WO2014125612 A1 WO 2014125612A1 JP 2013053693 W JP2013053693 W JP 2013053693W WO 2014125612 A1 WO2014125612 A1 WO 2014125612A1
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liquid
containing liquid
bubble
foam
bubbles
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PCT/JP2013/053693
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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 JP2013526022A priority Critical patent/JP5405693B1/en
Priority to PCT/JP2013/053693 priority patent/WO2014125612A1/en
Publication of WO2014125612A1 publication Critical patent/WO2014125612A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0021Degasification of liquids by bringing the liquid in a thin layer
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01JMANUFACTURE OF DAIRY PRODUCTS
    • A01J11/00Apparatus for treating milk
    • A01J11/04Appliances for aerating or de-aerating milk
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0036Flash degasification
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B2013/005Degassing undesirable residual components, e.g. gases, unreacted monomers, from material to be moulded

Definitions

  • the present invention includes various foods such as milk, soy milk, fruit juice, health supplements or nutritional agents, pharmaceuticals such as drinks, cosmetics such as facial liquids, hair washings, paints, battery pastes, other chemicals,
  • the present invention relates to a degassing method and apparatus for a bubble-containing liquid that removes and eliminates bubbles mixed in various liquid materials including viscous liquid materials such as polymer resins.
  • a degassing method and apparatus for a foam-containing liquid called a cyclone or a centrifugal separation method are known (for example, see Patent Document 1 and Patent Document 2).
  • the bubble separation device the bubble-containing liquid is caused to flow from the gap between the rotation shaft of the rotating tank and the surrounding through hole, and the bubbles in the liquid are taken out by flowing down on the guide member on the upper surface of the rotating tank, In addition, it is known to recover a liquid from which bubbles have been removed (see, for example, Patent Document 3).
  • a foam-containing liquid is discharged from a liquid film forming nozzle whose tip is reduced in diameter, and a liquid film having a circular shape in a plan view is formed after colliding with some member, It is known to take out bubbles in the liquid by reducing the pressure and collect the liquid from which the bubbles have been removed (see, for example, Patent Document 4).
  • the bubble separation device of Patent Document 3 does not have a configuration in which the liquid that has passed through the gap is bent in the direction of the rotation axis.
  • the vacuum deaerator of Patent Document 4 does not have a configuration in which the liquid flows in an annular shape in the liquid film forming nozzle.
  • the present applicant conducts the bubble-containing liquid that has been pressed and pressurized through a cylindrical tubular channel formed in one or more multi-annular tubular shapes so that bubbles in the liquid are long and adjacent bubbles. Disperse the polymer component into an expanded state, and once agglomerate directly or in the center, then expand it horizontally and circumferentially with respect to the center of the shaft to effectively separate the liquid component and the bubble component.
  • a gas component is removed and a degassed liquid component degassing method and apparatus have been developed (PCT / JP2012 / 063939 Japanese Patent Application No. 2012-540190). ).
  • the present invention further develops the above-described developed invention, and allows the bubble-containing liquid that has been pressed and pressurized to pass through one or more cylindrical tubular straight channels formed in a multi-ring shape so as to be contained in the liquid. Displace the bubbles in the outer circumference in the process of expanding and expanding the bubbles of the adjacent bubbles in an elongated manner, and discharging the discharge opening as a constricted configuration, separating and discharging the bubbles in the liquid, and easily It is an object of the present invention to provide a degassing method and apparatus for a foam-containing liquid that can efficiently remove a degassed liquid.
  • the present invention can solve the above problems by providing the following configuration.
  • a degassing method for a foam-containing liquid characterized by comprising a liquid diffusion step of expanding in an umbrella shape.
  • a foam-containing liquid pressurizing and supplying mechanism for supplying foam-containing liquid under pressure
  • a cylindrical laminar flow forming tube for introducing a bubble-containing liquid to be supplied under pressure, the laminar flow forming tube includes a cylindrical tube capable of forming an outer cylinder, and an inner layer formed at the center of the cylindrical tube.
  • the tubular layer flow path mechanism of the foam-containing liquid is any one of a polygon such as a triangle and a pentagon as well as a circular and elliptical cross section. Foam liquid deaerator.
  • the bubbles in the liquid are extended and rectified by diverting them to one or more annular tubular layers.
  • the bubbles in the liquid are compressed and simultaneously ejected to separate from the liquid into a vaporized state, which is very effectively separated from the liquid. .
  • the laminar flow state of the foam-containing liquid is 2 or more, the laminar flow action is expanded, the polymerization expansion of the gas component in each laminar flow is promoted, and the diversion action in each discharge part is increased, so that an efficient foam The liquid can be separated and taken out.
  • Sectional side view which shows an example of the defoaming apparatus which concerns on this invention II-II sectional view of FIG.
  • Cross-sectional explanatory drawing showing another embodiment of the present invention IV-IV sectional view of FIG.
  • FIGS. 1 and 2 First, the configuration of FIGS. 1 and 2 will be described.
  • Reference numeral 1 denotes a supply pipe of a foam-containing liquid supply mechanism 2 that pressurizes and supplies a foam-containing liquid
  • 3 denotes a foam-containing liquid stagnation part necessary for rectifying the foam-containing liquid supplied from the supply pipe 1 into a laminar flow
  • Reference numeral 4 denotes a laminar flow forming tube formed relatively longer than the bubble-containing liquid reservoir 3, and includes a cylindrical tube 5 forming an outer wall and an inner layer body 6 formed at the center of the cylindrical tube 5. And a tubular layer flow path mechanism 7 corresponding to the gap g is formed between the inner layer body 6 and the cylindrical tube 5.
  • This throttle structure is a narrow throttle discharge mechanism and can be formed by expanding or reducing the diameter of either the cylindrical tube 5 or the inner layer body 6.
  • Reference numeral 9 denotes an arc-shaped protruding portion that protrudes outward at the gas-liquid separation / discharge port 8 of the inner layer body 6, and the gas-liquid separated foam-containing liquid discharged from the gas-liquid separation / discharge port 8 Presents work to guide the direction.
  • a diffusion plate mechanism 10 is provided along the cylindrical tube 5 of the gas-liquid separation discharge port 8 for flowing down the umbrella-shaped separation liquid, and 11 is a detachment plate disposed on the outer periphery of the diffusion plate mechanism 10.
  • This is a liquid collection / reservation tank that can store the bubbled liquid, and the opening 12 of the liquid collection / reservation tank 11 is open to the atmosphere. It is also possible to perform suction under reduced pressure.
  • Reference numeral 13 denotes a discharge port, which measures the water level in the liquid recovery storage tank 11 so that it can be drained sequentially.
  • the cylindrical tube 5 of the laminar flow forming tube 4 is fixedly erected via the base 14 and an intermediate member, and the inner layer body 6 inserted into the cylindrical tube 5 has a conical portion at the tip.
  • the fixing rod 17 having the 15 inserted into the concave conical receiving body 16 and inserted through the center thereof can be inserted into the base 14 and fixed by a retaining ring 18 such as a nut.
  • 19 is a support rod for supporting the diffusion mechanism 10
  • 20 is a thumbscrew
  • 21 is a stop for supporting the substrate 14, and a movable pulley can be attached.
  • the bubble-containing liquid mixed with bubbles is supplied to the supply pipe 1 through the bubble-containing liquid supply mechanism 2 and introduced into the laminar flow forming tube 4.
  • the bubble-containing liquid immediately enters the bubble-containing liquid retention part 3 and is introduced into the tubular layer flow path mechanism 7 corresponding to the outer peripheral interval g, and is subjected to laminar flow action. Then, it is enlarged and reaches the gas-liquid separation discharge port 8, where the gap g is narrower and the squeezing effect works, and the foam-containing liquid is compressed and agglomerated and sprayed.
  • the gas component is separated from the liquid component, and is released to the atmosphere from the opening 12 of the liquid recovery storage tank 11.
  • the liquid component is led out toward the outer periphery by the arc-shaped protrusion 9, flows down along the umbrella-shaped diffusion plate mechanism 10 in a deaerated state, flows down and is stored in the liquid recovery storage tank 11, and is constant. After the amount storage, a degassed liquid can be obtained from the discharge port 13.
  • FIGS. 3 and 4 Next, the embodiment of FIGS. 3 and 4 will be described.
  • the gap g has a two-layer structure.
  • Cylindrical tubes 5a and 5b having different inner diameters are arranged on the outer periphery with the inner layer body 6 at the center.
  • 5b are provided with umbrella-shaped diffusion plate mechanisms 10a, 10b having substantially the same diameter and the same size.
  • a short time defoamed adapted to a large amount of bubble-containing liquid can be done efficiently. Since the other mechanism configuration is the same as that of the above-described embodiment, the same reference numerals are given and the detailed description is omitted.
  • the size of the double gaps g 1 and g 2 may be the same or different, and is not limited at all.
  • the length of the laminar flow forming tube 4 is preferably long, the length is not specified at all, and the cross-sectional shape of the laminar flow forming tube 4 is also circular or elliptical. It can be applied to polygonal shapes such as triangles and quadrangles as well as shapes.
  • the defoamed recovered liquid flowing out from the outer peripheral ends of the umbrella-shaped diffusion plate mechanisms 10, 10a, 10b is supplied into the liquid recovery storage tank 11 in a flowing state, but in order to avoid dripping.
  • a hanging plate (not shown) that assists the flow of the liquid can be attached to prevent the formation of a dripping situation that may generate bubbles.
  • the support rod 19a is held in the liquid recovery storage tank 11 with its upper end fixed.
  • the same configuration can be applied when forming a laminar flow of more than triple.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Animal Husbandry (AREA)
  • Environmental Sciences (AREA)
  • Degasification And Air Bubble Elimination (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

The present invention is a deaeration method for a bubble-containing liquid in which, using the laminar flow phenomenon that occurs when a liquid is made to move into a tube, air bubbles in the laminar flow are enlarged by aggregation and separated by discharge from a discharge opening to remove the bubbles. The dearation method is characterized by comprising the following: a bubble-containing liquid pressure-feed step in which a bubble-containing liquid is pressure fed; a single-layer or multiple-layer circulation pipe flow adjustment step in which the pressure-fed bubble-containing liquid can be subjected to thin-layer flow adjustment to the shape of a circulation pipe; a bubble enlargement step in which air bubbles in the bubble-containing liquid being transported during the aforementioned steps are pressurized by flow adjustment and are caused to flow together and enlarge; an air separation step in which, by constriction and release from a discharge opening, the air bubbles are separated and discharged from the liquid component; and a liquid diffusion step in which the liquid component separated from the air bubbles is made to diffuse in a radial umbrella shape.

Description

含泡液体の脱気方法及びその装置Method and apparatus for degassing foam-containing liquid
 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、その他の化成品、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除去排除する含泡液体の脱気方法及びその装置に関する。 The present invention includes various foods such as milk, soy milk, fruit juice, health supplements or nutritional agents, pharmaceuticals such as drinks, cosmetics such as facial liquids, hair washings, paints, battery pastes, other chemicals, The present invention relates to a degassing method and apparatus for a bubble-containing liquid that removes and eliminates bubbles mixed in various liquid materials including viscous liquid materials such as polymer resins.
 液体を最終製品とする技術分野は、食品、医療を始め高分子化学品など、その範囲はあらゆる物に及ぶ。 The technical field that uses liquids as final products covers a wide range of products, including food, medicine, and polymer chemicals.
 そして、液体製品であるため、濃度、精度などの物性上、混入又は発生する気泡は本質的に品質上多くの問題があり、排除することが不可避である。 And since it is a liquid product, there are many problems in terms of the quality of the bubbles that are mixed or generated due to physical properties such as concentration and accuracy, and it is inevitable to eliminate them.
 化学的に消泡剤を用いて行う場合もあるが、液体製品の品質管理上、悪影響を及ぼす場合が多く、一般的ではない。そこで多くの場合、機械的方法で脱泡する方法、装置が用いられている。 There are cases where chemicals are used chemically using an antifoaming agent, but there are many adverse effects on the quality control of liquid products, which is not common. Therefore, in many cases, a method and an apparatus for defoaming by a mechanical method are used.
 具体的には、サイクロンないし遠心分離方式と呼ばれる含泡液体の脱気方法やその装置が知られている(例えば、特許文献1、特許文献2参照)。 Specifically, a degassing method and apparatus for a foam-containing liquid called a cyclone or a centrifugal separation method are known (for example, see Patent Document 1 and Patent Document 2).
 さらに、気泡分離装置に関し、含泡液体を回転タンクの回転軸とその周囲の貫通孔との間隙より流入させ、回転タンクの上面のガイド部材上を流下させることで、液体中の気泡を取り出し、また、気泡が取り除かれた液体を回収することが知られている(例えば、特許文献3参照)。 Furthermore, regarding the bubble separation device, the bubble-containing liquid is caused to flow from the gap between the rotation shaft of the rotating tank and the surrounding through hole, and the bubbles in the liquid are taken out by flowing down on the guide member on the upper surface of the rotating tank, In addition, it is known to recover a liquid from which bubbles have been removed (see, for example, Patent Document 3).
 さらにまた、塗布装置に用いられる真空脱泡装置に関し、含泡液体を先端が縮径した液膜形成ノズルから放出し、なんらかの部材に衝突させた上で平面視円形状の液膜を形成し、減圧により液体中の気泡を取り出し、また、気泡が取り除かれた液体を回収することが知られている(例えば、特許文献4参照)。 Furthermore, regarding a vacuum defoaming apparatus used for a coating apparatus, a foam-containing liquid is discharged from a liquid film forming nozzle whose tip is reduced in diameter, and a liquid film having a circular shape in a plan view is formed after colliding with some member, It is known to take out bubbles in the liquid by reducing the pressure and collect the liquid from which the bubbles have been removed (see, for example, Patent Document 4).
特開2006-27012号公報JP 2006-27012 A 特開平10-43293号公報JP 10-43293 A 特開昭57-197004号公報JP-A-57-197004 特開2006-122812号公報JP 2006-122812 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 swirl flow passage. In addition, a cylindrical filter body provided in the center is installed to separate the bubbles and separate them from the liquid, and the deaeration is controlled simply by the mesh size and the size of the filter body. The problem of being inevitable is inevitable.
 また、上記特許文献3の気泡分離装置においては、間隙を通過した液体が回転軸の方向へと曲折されるような構成を有するものではない。 Further, the bubble separation device of Patent Document 3 does not have a configuration in which the liquid that has passed through the gap is bent in the direction of the rotation axis.
 さらに、上記特許文献4の真空脱泡装置においては、液膜形成ノズル内において、液体が環管状に流れる構成を有するものではない。 Furthermore, the vacuum deaerator of Patent Document 4 does not have a configuration in which the liquid flows in an annular shape in the liquid film forming nozzle.
 これに対し、本出願人は、押圧加圧された被含泡液体を一層以上の多重環管状に形成される円筒管状の流路に導通させて液体中の気泡分を長尺かつ隣り合う気泡分を重合させて拡開させた状態に変位させ、直接又は中央で一旦凝集させた後、軸中心に対して水平方向、円周方向に拡張して液体分と気泡分とを有効に分離して、排出後は気体分を除去させると共に、脱気状態の液体分を取り出せるようにした含泡液体の脱気方法及びその装置を開発した事実がある(PCT/JP2012/063939 特願2012-540190)。 On the other hand, the present applicant conducts the bubble-containing liquid that has been pressed and pressurized through a cylindrical tubular channel formed in one or more multi-annular tubular shapes so that bubbles in the liquid are long and adjacent bubbles. Disperse the polymer component into an expanded state, and once agglomerate directly or in the center, then expand it horizontally and circumferentially with respect to the center of the shaft to effectively separate the liquid component and the bubble component. In addition, there is a fact that after the discharge, a gas component is removed and a degassed liquid component degassing method and apparatus have been developed (PCT / JP2012 / 063939 Japanese Patent Application No. 2012-540190). ).
 本発明は上述した開発した発明をさらに発展させて、押圧加圧された被含泡液体を一層ないし一層以上の多重環管状に形成される円筒管状の直状の流路に導通させて液体中の気泡分を長尺かつ隣り合う気泡分を重合させて拡開させた過程で外周方向に変位させ、かつ吐出開口部分を絞り構成として吐出させ、液体中の気泡部分を分離吐出排気し、簡単効率的に脱気状態の液体分を取り出せるようにした含泡液体の脱気方法及びその装置を提供することを目的とする。 The present invention further develops the above-described developed invention, and allows the bubble-containing liquid that has been pressed and pressurized to pass through one or more cylindrical tubular straight channels formed in a multi-ring shape so as to be contained in the liquid. Displace the bubbles in the outer circumference in the process of expanding and expanding the bubbles of the adjacent bubbles in an elongated manner, and discharging the discharge opening as a constricted configuration, separating and discharging the bubbles in the liquid, and easily It is an object of the present invention to provide a degassing method and apparatus for a foam-containing liquid that can efficiently remove a degassed liquid.
 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)含泡液体を加圧供給する含泡液体加圧供給工程、加圧供給される含泡液体を環管状に薄層整流できる一層ないし多層の環管整流工程、前記工程中に移送中の含泡液体中の気泡を整流加圧して合流拡大させる気泡拡大工程、排出口より絞り開放させて気泡を液体分より分離排出させる気体分離工程、及び前記気泡と分離された液体分を放射状の傘状に拡開させる液体拡散工程とより成ることを特徴とする含泡液体の脱気方法。 (1) A foam-containing liquid pressurizing and supplying step for supplying foam-containing liquid under pressure, a one-layer or multi-layer ring-tube rectifying step capable of thin-layer rectifying the foam-containing liquid supplied under pressure, and being transferred during the step A bubble expanding step of rectifying and pressurizing bubbles in the bubble-containing liquid and converging and expanding, a gas separation step of separating and discharging bubbles from the liquid by opening the throttle from the discharge port, and a radial separation of the liquid separated from the bubbles A degassing method for a foam-containing liquid, characterized by comprising a liquid diffusion step of expanding in an umbrella shape.
 (2)含泡液体を加圧供給する含泡液体加圧供給機構と、
 加圧供給される含泡液体を導入する筒体の層流形成管体と、該層流形成管体は、外筒を形成できる円筒管と、この円筒管の中央に形成される内層体を備え、一以上の間隙を介して形成されて内部に配設される環管状の含泡液体の管状層流路機構と、
 該管状層流路機構の吐出側に含泡液体を絞る、狭少にした気液分離吐出口機構と、
 前記機構で吐出された気泡を排気分離した液体分を流下させる拡散板機構と、
 脱気液体を静止回収貯溜する液体回収貯溜槽機構と、
を備えることを特徴とする含泡液体の脱気装置。
(2) a foam-containing liquid pressurizing and supplying mechanism for supplying foam-containing liquid under pressure;
A cylindrical laminar flow forming tube for introducing a bubble-containing liquid to be supplied under pressure, the laminar flow forming tube includes a cylindrical tube capable of forming an outer cylinder, and an inner layer formed at the center of the cylindrical tube. A tubular layer flow path mechanism of an annular tubular foam-containing liquid formed through one or more gaps and disposed therein;
A narrow gas-liquid separation outlet mechanism that squeezes the foam-containing liquid to the discharge side of the tubular layer flow path mechanism;
A diffusion plate mechanism for flowing down a liquid component obtained by exhausting and separating bubbles discharged by the mechanism;
A liquid recovery and storage tank mechanism for stationary recovery and storage of degassed liquid;
A degassing device for a foam-containing liquid, comprising:
 (3)含泡液体の管状層流路機構の導入部には含泡液体を導入保持する含泡液体貯溜部を設けて成ることを特徴とする前記(2)記載の含泡液体の脱気装置。 (3) The degassing of the foam-containing liquid according to (2), wherein the foam-containing liquid storage section for introducing and holding the foam-containing liquid is provided in the introduction section of the tubular layer flow path mechanism of the foam-containing liquid. apparatus.
 (4)含泡液体の管状層流路機構の間隙には、一層ないし多層の含泡液体の流路を形成して成ることを特徴とする前記(2)記載の含泡液体の脱気装置。 (4) The bubble-containing liquid deaeration device according to (2), wherein a single-layer or multi-layer flow path of the bubble-containing liquid is formed in the gap of the tubular layer flow path mechanism of the bubble-containing liquid. .
 (5)狭少絞り吐出機構には、気体を分離された液体を流下させる傘機構を備えて成ることを特徴とする前記(2)記載の含泡液体の脱気装置。 (5) The bubble-containing liquid deaeration device according to (2), wherein the narrow-throttle discharge mechanism is provided with an umbrella mechanism for flowing down the liquid from which the gas has been separated.
 (6)狭少絞り吐出機構は、円筒管又は内層体のいずれか一方を拡幅又は縮径させて絞り構成として成ることを特徴とする前記(2)記載の含泡液体の脱気装置。 (6) The degassing device for a foam-containing liquid according to (2), wherein the narrow throttle discharge mechanism has a throttle configuration by widening or reducing the diameter of either the cylindrical tube or the inner layer body.
 (7)含泡液体の管状層流路機構は、断面円形、楕円形は勿論のこと、三角形、五角形などの多角形のいずれか一つであることを特徴とする前記(2)記載の含泡液体の脱気装置。 (7) The tubular layer flow path mechanism of the foam-containing liquid is any one of a polygon such as a triangle and a pentagon as well as a circular and elliptical cross section. Foam liquid deaerator.
 (8)液体回収貯溜槽機構には、排気された気体を吸引排除する減圧機構を備えて成ることを特徴とする前記(2)記載の含泡液体の脱気装置。 (8) The degassing apparatus for a foam-containing liquid according to (2), wherein the liquid recovery and storage tank mechanism is provided with a pressure reducing mechanism for sucking and exhausting the exhausted gas.
 本発明に拠れば、含泡流体を加圧移送させる際、環管状の1層ないし2以上の多層に分流させて液体中の気泡を伸長させ、かつ整流させているので、隣り合う気泡同士が合流合体して拡張し、吐出排出口部分の絞り作用を経て、液体分中の気泡は圧縮されると同時に噴出作用を経て、液体より分離して気化状態となり、極めて有効に液体と分離される。 According to the present invention, when the foam-containing fluid is pressurized and transferred, the bubbles in the liquid are extended and rectified by diverting them to one or more annular tubular layers. Combined and expanded, and through the squeezing action of the discharge / discharge port, the bubbles in the liquid are compressed and simultaneously ejected to separate from the liquid into a vaporized state, which is very effectively separated from the liquid. .
 含泡液体の層流状態が2以上であれば層流作用は拡大し、各層流での気体分の重合拡大が促進れ、それぞれの吐出部での分流作用が増大して効率的な泡体、液体との分離取り出しを行うことが可能となる。 If the laminar flow state of the foam-containing liquid is 2 or more, the laminar flow action is expanded, the polymerization expansion of the gas component in each laminar flow is promoted, and the diversion action in each discharge part is increased, so that an efficient foam The liquid can be separated and taken out.
本発明に係る脱泡装置の一例を示す断面側面図Sectional side view which shows an example of the defoaming apparatus which concerns on this invention 図1のII-II線断面図II-II sectional view of FIG. 本発明の他の実施例を示す断面説明図Cross-sectional explanatory drawing showing another embodiment of the present invention 図3のIV-IV線断面図IV-IV sectional view of FIG.
 以下、本発明を実施するための最良の形態を実施例により詳しく説明する。 Hereinafter, the best mode for carrying out the present invention will be described in detail with reference to examples.
 以下、本発明の一実施例を図面と共に説明する。 Hereinafter, an embodiment of the present invention will be described with reference to the drawings.
 はじめに、図1及び図2の構成について説明する。 First, the configuration of FIGS. 1 and 2 will be described.
 1は、含泡液体を加圧供給する含泡液体供給機構2の供給管、3は供給管1より供給される含泡液体を層流に整流するために必要な含泡液体滞溜部、4は前記含泡液体滞溜部3より比較的長尺に形成される層流形成管体であって、外壁を形成する円筒管5及びこの円筒管5の中央に形成される内層体6を備え、この内層体6と前記円筒管5との間に間隙gに相当する管状層流路機構7を形成する。 Reference numeral 1 denotes a supply pipe of a foam-containing liquid supply mechanism 2 that pressurizes and supplies a foam-containing liquid, 3 denotes a foam-containing liquid stagnation part necessary for rectifying the foam-containing liquid supplied from the supply pipe 1 into a laminar flow Reference numeral 4 denotes a laminar flow forming tube formed relatively longer than the bubble-containing liquid reservoir 3, and includes a cylindrical tube 5 forming an outer wall and an inner layer body 6 formed at the center of the cylindrical tube 5. And a tubular layer flow path mechanism 7 corresponding to the gap g is formed between the inner layer body 6 and the cylindrical tube 5.
 8は、前記層流形成管体4の含泡液体の吐出側に形成される気液分離吐出口であって、間隙gを狭少にすべく絞り構造として形成してある。この絞り構造は、狭少絞り吐出機構であって、円筒管5又は内層体6のいずれか一方を拡幅又は縮径させて形成できる。9は内層体6の気液分離吐出口8において外方に突出させた弧状突出部であって、気液分離吐出口8より吐出される気液分離状態の含泡液体を、外方円周方向に案内させるための働きを呈する。 8 is a gas-liquid separation and discharge port formed on the discharge side of the bubble-containing liquid of the laminar flow forming tube 4 and is formed as a throttle structure so as to narrow the gap g. This throttle structure is a narrow throttle discharge mechanism and can be formed by expanding or reducing the diameter of either the cylindrical tube 5 or the inner layer body 6. Reference numeral 9 denotes an arc-shaped protruding portion that protrudes outward at the gas-liquid separation / discharge port 8 of the inner layer body 6, and the gas-liquid separated foam-containing liquid discharged from the gas-liquid separation / discharge port 8 Presents work to guide the direction.
 10は、前記気液分離吐出口8の円筒管5に沿って設けた、傘状の分離液体を流下させるための拡散板機構、11は、前記拡散板機構10の外周に配設される脱泡された液体を収容できる液体回収貯溜槽であって、この液体回収貯溜槽11の開口部12は大気開放となっているが、必要に応じて蓋による遮蔽構造とし図示しないが、減圧モータなどにより減圧吸引することも可能である。13は排出口であって、液体回収貯溜槽11内の水位を計測して順次排水可能としている。 A diffusion plate mechanism 10 is provided along the cylindrical tube 5 of the gas-liquid separation discharge port 8 for flowing down the umbrella-shaped separation liquid, and 11 is a detachment plate disposed on the outer periphery of the diffusion plate mechanism 10. This is a liquid collection / reservation tank that can store the bubbled liquid, and the opening 12 of the liquid collection / reservation tank 11 is open to the atmosphere. It is also possible to perform suction under reduced pressure. Reference numeral 13 denotes a discharge port, which measures the water level in the liquid recovery storage tank 11 so that it can be drained sequentially.
 また、上記構成において、層流形成管体4の円筒管5は、基盤14と中間部材などを介して固定起立され、前記円筒管5内に挿通される内層体6は、先端の円錐状部15を凹状型円錐状受体16に係入させ、かつ中心に挿通させた固定棒17を、基盤14内に挿通させてナットなどの止環18で固定して組立てることができる。 Further, in the above configuration, the cylindrical tube 5 of the laminar flow forming tube 4 is fixedly erected via the base 14 and an intermediate member, and the inner layer body 6 inserted into the cylindrical tube 5 has a conical portion at the tip. The fixing rod 17 having the 15 inserted into the concave conical receiving body 16 and inserted through the center thereof can be inserted into the base 14 and fixed by a retaining ring 18 such as a nut.
 なお、19は前記拡散機構10を支持する支持杆、20はその蝶ねじ、21は基板14を支持する止杆であって、移動可能な自在滑車を付設することもできる。 In addition, 19 is a support rod for supporting the diffusion mechanism 10, 20 is a thumbscrew, 21 is a stop for supporting the substrate 14, and a movable pulley can be attached.
 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.
 気泡を混入する含泡液体は、含泡液体供給機構2を経て、供給管1に供給されて、層流形成管体4へ導入される。含泡液体は直ちに含泡液体滞溜部3に入り、外周の間隔gに相当する管状層流路機構7に導入され、層流作用を受け、液体内の気泡は互いに隣り合う気泡同士が結合し、拡大されて気液分離吐出口8に達し、ここで間隔gがより狭少で絞り効果が働き、含泡液体が圧縮凝集して噴霧吐出される。気体分は液体分より離散し、液体回収貯溜槽11の開口部12より大気開放される。液体分は、弧状突出部9によって外方外周に向かって導出され、脱気された状態で傘状の拡散板機構10に沿って流下し、液体回収貯溜槽11内に流下し貯溜され、一定量貯溜後、排出口13より脱気状態の液体を得ることができる。 The bubble-containing liquid mixed with bubbles is supplied to the supply pipe 1 through the bubble-containing liquid supply mechanism 2 and introduced into the laminar flow forming tube 4. The bubble-containing liquid immediately enters the bubble-containing liquid retention part 3 and is introduced into the tubular layer flow path mechanism 7 corresponding to the outer peripheral interval g, and is subjected to laminar flow action. Then, it is enlarged and reaches the gas-liquid separation discharge port 8, where the gap g is narrower and the squeezing effect works, and the foam-containing liquid is compressed and agglomerated and sprayed. The gas component is separated from the liquid component, and is released to the atmosphere from the opening 12 of the liquid recovery storage tank 11. The liquid component is led out toward the outer periphery by the arc-shaped protrusion 9, flows down along the umbrella-shaped diffusion plate mechanism 10 in a deaerated state, flows down and is stored in the liquid recovery storage tank 11, and is constant. After the amount storage, a degassed liquid can be obtained from the discharge port 13.
 つぎに、図3及び図4の実施例について説明する。 Next, the embodiment of FIGS. 3 and 4 will be described.
 この実施例は間隙gが2層構成としたもので、内層体6を中心として外周に二重の内径を異にした円筒管5a,5bを配設したもので、之等の内周管5a,5bの端縁には略同径同大の傘状の拡散板機構10a,10bを設けるものである。 In this embodiment, the gap g has a two-layer structure. Cylindrical tubes 5a and 5b having different inner diameters are arranged on the outer periphery with the inner layer body 6 at the center. , 5b are provided with umbrella-shaped diffusion plate mechanisms 10a, 10b having substantially the same diameter and the same size.
 そして、層流形成管体4Aの外周部分に二重の間隙g,gを設けた管状層流路機構7a,7bを形成し、多量の含泡液体に適応した脱泡処理を短時間に能率よく行わせることができる。その他の機構構成は、前記実施例と同一であるので、同一符号を施し説明の詳細を省く。ここで、二重の間隙g,gの大きさは同一でも異なっても良く、何等限定されない。 Then, the outer peripheral portion in a double gap g 1, g 2 a provided tubular layer flow channel mechanism 7a of laminar flow formed tube 4A, 7b is formed, a short time defoamed adapted to a large amount of bubble-containing liquid Can be done efficiently. Since the other mechanism configuration is the same as that of the above-described embodiment, the same reference numerals are given and the detailed description is omitted. Here, the size of the double gaps g 1 and g 2 may be the same or different, and is not limited at all.
 なお、上記実施例において、層流形成管体4の長さは長尺であることが好ましく、その長さは何等特定されず、また、同層流形成管体4の断面形状も円形,楕円形は勿論のこと、三角形,四角形などの多角形状について実施できる。 In the above embodiment, the length of the laminar flow forming tube 4 is preferably long, the length is not specified at all, and the cross-sectional shape of the laminar flow forming tube 4 is also circular or elliptical. It can be applied to polygonal shapes such as triangles and quadrangles as well as shapes.
 そして、傘状の拡散板機構10,10a,10bの外周端より流出する脱泡された回収液体は流下状態で液体回収貯溜槽11内に供給されるものであるが、滴下の場合を避けるため、液体の流下を助ける吊下板(図示せず)を付設して気泡を発生する虞れのある滴下状況の形成を防止することもできる。 The defoamed recovered liquid flowing out from the outer peripheral ends of the umbrella-shaped diffusion plate mechanisms 10, 10a, 10b is supplied into the liquid recovery storage tank 11 in a flowing state, but in order to avoid dripping. In addition, a hanging plate (not shown) that assists the flow of the liquid can be attached to prevent the formation of a dripping situation that may generate bubbles.
 さらに、支持杆19に代えて、支持杆19aを液体回収貯溜槽11に上端を固着して保持している。 Furthermore, instead of the support rod 19, the support rod 19a is held in the liquid recovery storage tank 11 with its upper end fixed.
 また、三重以上の層流を形成する場合も同様の構成で実施できる。 Also, the same configuration can be applied when forming a laminar flow of more than triple.
 1       供給管
 2       含泡液体供給機構
 3       含泡液体滞溜部
 4,4A    層流形成管体
 5,5a,5b 円筒管
 6       内層体
 7,7a,7b 管状層流路機構
 8       気液分離吐出口
 9       弧状突出部
 10,10a,10b 拡散板機構
 11      液体回収貯溜槽
 12      開口部
 13      排出口
 14      基盤
 15      円錐状部
 16      凹状型円錐状受体
 17      固定棒
 18      止環
 19,19a  支持杆
 20      蝶ねじ
 21      止杆
 g,g,g  間隙
DESCRIPTION OF SYMBOLS 1 Supply pipe 2 Foam-containing liquid supply mechanism 3 Foam-containing liquid retention part 4, 4A Laminar flow formation tube 5, 5a, 5b Cylindrical tube 6 Inner layer 7, 7a, 7b Tubular layer flow-path mechanism 8 Gas-liquid separation discharge port DESCRIPTION OF SYMBOLS 9 Arc-shaped protrusion 10, 10a, 10b Diffusion board mechanism 11 Liquid collection | recovery storage tank 12 Opening part 13 Outlet 14 Base 15 Conical part 16 Concave-shaped conical receiving body 17 Fixing rod 18 Retaining ring 19, 19a Supporting rod 20 Butterfly screw 21 Stop g, g 1 , g 2 gap

Claims (8)

  1.  含泡液体を加圧供給する含泡液体加圧供給工程、加圧供給される含泡液体を環管状に薄層整流できる一層ないし多層の環管整流工程、前記工程中に移送中の含泡液体中の気泡を整流加圧して合流拡大させる気泡拡大工程、排出口より絞り開放させて気泡を液体分より分離排出させる気体分離工程、及び前記気泡と分離された液体分を放射状の傘状に拡開させる液体拡散工程とより成ることを特徴とする含泡液体の脱気方法。 Foamed liquid pressurizing and supplying step for supplying foamed liquid under pressure, one to multi-layered ring rectifying step capable of thinly rectifying the foamed liquid supplied under pressure into an annular shape, foaming during transfer during the process Bubble expansion process for rectifying and pressurizing bubbles in the liquid to expand the confluence, gas separation process for separating and discharging the bubbles from the liquid by opening the throttle from the discharge port, and the liquid component separated from the bubbles in a radial umbrella shape A degassing method for a foam-containing liquid, comprising a liquid diffusion step of spreading.
  2.  含泡液体を加圧供給する含泡液体加圧供給機構と、
     加圧供給される含泡液体を導入する筒体の層流形成管体と、該層流形成管体は、外筒を形成できる円筒管と、この円筒管の中央に形成される内層体を備え、一以上の間隙を介して形成されて内部に配設される環管状の含泡液体の管状層流路機構と、
     該管状層流路機構の吐出側に含泡液体を絞る、狭少にした気液分離吐出口機構と、
     前記機構で吐出された気泡を排気分離した液体分を流下させる拡散板機構と、
     脱気液体を静止回収貯溜する液体回収貯溜槽機構と、
    を備えることを特徴とする含泡液体の脱気装置。
    A foam-containing liquid pressurizing and supplying mechanism for supplying foam-containing liquid under pressure;
    A cylindrical laminar flow forming tube for introducing a bubble-containing liquid to be supplied under pressure, the laminar flow forming tube includes a cylindrical tube capable of forming an outer cylinder, and an inner layer formed at the center of the cylindrical tube. A tubular layer flow path mechanism of an annular tubular foam-containing liquid formed through one or more gaps and disposed therein;
    A narrow gas-liquid separation outlet mechanism that squeezes the foam-containing liquid to the discharge side of the tubular layer flow path mechanism;
    A diffusion plate mechanism for flowing down a liquid component obtained by exhausting and separating bubbles discharged by the mechanism;
    A liquid recovery and storage tank mechanism for stationary recovery and storage of degassed liquid;
    A degassing device for a foam-containing liquid, comprising:
  3.  含泡液体の管状層流路機構の導入部には含泡液体を導入保持する含泡液体貯溜部を設けて成ることを特徴とする請求項2記載の含泡液体の脱気装置。 3. The deaerator for foamed liquid according to claim 2, wherein a foamed liquid reservoir for introducing and holding the foamed liquid is provided at the introduction part of the tubular layer flow path mechanism of the foamed liquid.
  4.  含泡液体の管状層流路機構の間隙には、一層ないし多層の含泡液体の流路を形成して成ることを特徴とする請求項2記載の含泡液体の脱気装置。 3. The bubble-containing liquid deaeration apparatus according to claim 2, wherein a single or multi-layer bubble-containing liquid channel is formed in the gap of the bubble-containing liquid tubular layer flow path mechanism.
  5.  狭少絞り吐出機構には、気体を分離された液体を流下させる傘機構を備えて成ることを特徴とする請求項2記載の含泡液体の脱気装置。 3. The bubble-containing liquid deaeration device according to claim 2, wherein the narrow-throttle discharge mechanism is provided with an umbrella mechanism for flowing down the liquid from which the gas is separated.
  6.  狭少絞り吐出機構は、円筒管又は内層体のいずれか一方を拡幅又は縮径させて絞り構成として成ることを特徴とする請求項2記載の含泡液体の脱気装置。 3. The degassing device for foamed liquid according to claim 2, wherein the narrow throttle discharge mechanism has a throttle configuration by widening or reducing the diameter of either the cylindrical tube or the inner layer body.
  7.  含泡液体の管状層流路機構は、断面円形、楕円形は勿論のこと、三角形、五角形などの多角形のいずれか一つであることを特徴とする請求項2記載の含泡液体の脱気装置。 3. The bubble-containing liquid removal mechanism according to claim 2, wherein the bubble-containing liquid tubular layer flow path mechanism is any one of a polygon such as a triangle and a pentagon as well as a circular and elliptical cross section. Qi device.
  8.  液体回収貯溜槽機構には、排気された気体を吸引排除する減圧機構を備えて成ることを特徴とする請求項2記載の含泡液体の脱気装置。 3. The degassing device for a foam-containing liquid according to claim 2, wherein the liquid collection and storage tank mechanism is provided with a pressure reducing mechanism for sucking and exhausting the exhausted gas.
PCT/JP2013/053693 2013-02-15 2013-02-15 Deaeration method for bubble-containing liquid and device therefor WO2014125612A1 (en)

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