JP2014079726A - Method and device of deaerating foam-containing liquid - Google Patents

Method and device of deaerating foam-containing liquid Download PDF

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JP2014079726A
JP2014079726A JP2012231005A JP2012231005A JP2014079726A JP 2014079726 A JP2014079726 A JP 2014079726A JP 2012231005 A JP2012231005 A JP 2012231005A JP 2012231005 A JP2012231005 A JP 2012231005A JP 2014079726 A JP2014079726 A JP 2014079726A
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liquid
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containing liquid
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JP5548250B2 (en
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Koichi Arai
孝一 荒井
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Arai Machinery Corp
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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
    • B01D19/0026Degasification of liquids by bringing the liquid in a thin layer in rotating vessels or in vessels containing movable parts

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Abstract

PROBLEM TO BE SOLVED: To provide a method and device of deaerating a foam-containing liquid for taking out the liquid content in a deaerated state by: conducting a pressed-pressurized foam-containing liquid through a flow passage formed in a multiple annular tube shape; displacing the foam content in liquid in an expansively opened state by superposing the long and adjacent foam content; separating the liquid content and the gas content by expanding the foam-containing liquid in the horizontal direction to the axial center after coagulating the foam-containing liquid once in the center; and removing the gas content by an exhaust mechanism under atmospheric pressure after discharge.SOLUTION: The method of deaerating the foam-containing liquid includes: a foam-containing liquid pressure feeding process of pressure feeding the foam-containing liquid; a one- or multi-layer annular tube rectifying process of rectifying the pressurized-supplied foam-containing liquid into a thin layer in an annular tube shape; a bending/coagulation process of coagulating and horizontally bending the foam-containing liquid on the downstream side of the central axis of an annular tube flow passage of the pressure-fed foam-containing liquid; a gas-liquid separation process of separating foam from the liquid by collecting-expanding the adjacent foam in the foam-containing liquid by forming the foam-containing liquid in the thin layer and expanding it in a circumferential planar shape; an exhaust process under the atmospheric pressure for taking out the foam in the liquid; and a liquid sampling process of collecting exhaust liquid.

Description

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 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 degassing method and apparatus for a bubble-containing liquid that eliminates bubbles mixed in various liquid materials including a viscous liquid material.

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 of using 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, the bubble which mixes or generate | occur | produces from a physical property, such as a density | concentration and an accuracy, has many problems on quality essentially, and it is inevitable to eliminate.

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。   Although it may be performed chemically using an antifoaming agent, it often has an adverse effect on the quality control of liquid products and is not general. 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 (see, for example, 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記載されている(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, Further, it is described that the liquid from which bubbles are removed is recovered (for example, see 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記載されている(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 described that bubbles in the liquid are taken out by decompression and the liquid from which the bubbles are removed is recovered (for example, see Patent Document 4).

特開2006−27012号公報JP 2006-27012 A 特開平10−43293号公報JP-A-10-43293 特開昭57−197004号公報JP 57-197004 A 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 both of Patent Documents 1 and 2 mentioned 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.

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。   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。   Further, the vacuum defoaming device of Patent Document 4 does not have a configuration in which the liquid flows in an annular shape in the liquid film forming nozzle.

本発明は、叙上の点に着目して成されたもので、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周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、排出後は減圧吸気機構を用いることなく大気圧下の排気機構で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提供することを目的とする。   The present invention has been made by paying attention to the above points, and allows the bubble-containing liquid that has been pressed and pressurized to pass through a circumferential tubular channel formed in one or more multi-annular tubular forms. Disperse the bubbles in the long and adjacent bubbles to the expanded state, and after agglomerating directly or in the center, the liquid is expanded horizontally and circumferentially with respect to the axis center. A bubble-containing liquid that effectively separates the air and air bubbles, and after discharge, removes the gas with an exhaust mechanism under atmospheric pressure without using a vacuum intake mechanism, and allows the degassed liquid to be removed. An object of the present invention is to provide a deaeration method and an apparatus therefor.

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、
加圧供給される含泡液体の環管流路の中心軸の下流に含泡液体を凝集させると共に水平方向に曲折させる曲折凝集工程、
含泡液体を薄層に形成して円周平面状に拡大して含泡液体中の隣り合う気泡を集合拡大して液体との分離を行わせるようにした気液分離工程、
液体中の気泡を取り出す大気圧下排気工程、
排気液体を集める液体採取工程、
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 single-layer or multi-layer ring rectification process capable of thinly rectifying a bubble-containing liquid supplied under pressure into an annular shape;
A bending agglomeration step for aggregating the foamed liquid downstream of the central axis of the annular flow path of the foamed liquid to be supplied under pressure and bending it in the horizontal direction;
A gas-liquid separation step in which a foam-containing liquid is formed into a thin layer and expanded in a circumferential plane to collect and expand adjacent bubbles in the foam-containing liquid to separate them from the liquid,
An exhaust process under atmospheric pressure to extract bubbles in the liquid,
Liquid collection process for collecting exhaust liquid,
A degassing method for a foam-containing liquid, comprising:

(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円筒体の円筒体壁と、間隙を介して形成されて内部に配設される中央膨出体との間の環管状の含泡液体の管状拡張液路機構と、
含泡液体を前記中央膨出体の中心軸の下流に集合させて水平方向に曲折させる曲折凝集機構と、
凝集された含泡液体を円周平面状に拡大させて含泡液体中の気泡を拡大させて、液体と分離できる円周拡大拡散機構と、
液体と分離した気泡を大気中に排気できる大気圧下排気機構と、
脱気液体を静止貯溜する機構と、
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;
Tubular expansion liquid of a ring-shaped foam-containing liquid between a cylindrical body wall for introducing a foam-containing liquid to be supplied under pressure and a central bulging body formed through a gap and disposed inside Road mechanism,
A bending and aggregating mechanism for collecting the foam-containing liquid downstream of the central axis of the central bulging body and bending it in the horizontal direction;
A circumferentially expanding diffusion mechanism that expands the agglomerated foamed liquid in a circumferential plane to expand the bubbles in the foamed liquid, and can be separated from the liquid;
An atmospheric pressure exhaust mechanism capable of exhausting air bubbles separated from liquid into the atmosphere;
A mechanism for stationary storage of degassed liquid;
A degassing device for a foam-containing liquid, comprising:

(3)含泡液体の管状拡張液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 mechanism for introducing and holding the foam-containing liquid is provided in the introduction section of the tubular expanded liquid path mechanism of the foam-containing liquid. apparatus.

(4)含泡液体の管状拡張液路機構の間隙で形成される含泡液体の流路の大きさには、段差部を設けて上流側に対して下流側を小さくして狭搾り作用を増大できるようにして成ることを特徴とする前記(2)記載の含泡液体の脱気装置。   (4) The size of the flow path of the foam-containing liquid formed in the gap of the tubular expanded liquid path mechanism of the foam-containing liquid is provided with a stepped portion so that the downstream side is smaller than the upstream side and the squeezing action is achieved. The degassing device for a foam-containing liquid according to the above (2), characterized in that it can be increased.

(5)含泡液体の管状拡張液路機構の間隙には、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)又は(4)記載の含泡液体の脱気装置。   (5) The foam-containing liquid as described in (2) or (4) above, wherein a single-layer or multi-layer flow path of the foam-containing liquid is formed in the gap of the tubular expanded liquid path mechanism of the foam-containing liquid. Deaeration device.

本発明に拠れば、含泡液体を加圧移送させる手段と、一層ないし多層の円管構成で流通路幅を細少して液体中の気泡を円周平面方向に拡大拡開させ凝集させること、並びに減圧吸引手段を用いないで含泡液体の加圧供給手段によって大気圧下に直接気化された気泡を排除できるので構成が簡単で組立が容易であり、特に粘稠度の少ない含泡液体に有効であるなど、全体の構成が簡単に形成して消泡、脱泡を必要とする製造ラインに組み込むことができる。   According to the present invention, a means for pressurizing and transporting the foam-containing liquid, and the flow path width is narrowed by a single or multi-layered circular tube configuration to expand and expand the bubbles in the liquid in the circumferential plane direction, In addition, since the bubbles directly vaporized under atmospheric pressure can be eliminated by the pressure supply means of the foam-containing liquid without using the vacuum suction means, the structure is simple and the assembly is easy, and the foam-containing liquid with particularly low viscosity is used. The entire configuration can be formed easily and incorporated into a production line that requires defoaming and defoaming.

本発明に係る脱泡装置の断面説明図Cross-sectional explanatory drawing of a defoaming apparatus according to the present invention 図1のII−II線断面図II-II sectional view of FIG. 図1のIII−III線断面図III-III 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.

以下に本発明の一実施例を図面と共に説明する。   An embodiment of the present invention will be described below with reference to the drawings.

1は含泡液体を加圧供給する含泡液体加圧供給機構2の供給管、3は含泡液体を導入保持する含泡液体貯溜部、4は前記含泡液体貯溜部3に続く環管状の含泡液体の管状拡張流路機構を示し、中空状の円筒体5の上部には前記含泡液体貯溜部3が形成され、円筒体5の内部に配設される両端を固定して中央部分が膨出拡大した構成の中央膨出体6の外周面6aと円筒体5の内周面5aとの間に形成される間隙gにこの含泡液体の管状拡張流路機構4(流路)が形成される。   Reference numeral 1 denotes a supply pipe of a foam-containing liquid pressurizing and supplying mechanism 2 that pressurizes and supplies the foam-containing liquid, 3 denotes a foam-containing liquid reservoir for introducing and holding the foam-containing liquid, and 4 denotes an annular tube following the foam-containing liquid reservoir 3. FIG. 2 shows a tubular expanded flow path mechanism for the foam-containing liquid, wherein the foam-containing liquid reservoir 3 is formed in the upper part of the hollow cylindrical body 5, and both ends disposed inside the cylindrical body 5 are fixed to the center. This bubble-containing liquid tubular expansion channel mechanism 4 (channel) is formed in a gap g formed between the outer peripheral surface 6a of the central bulging body 6 and the inner peripheral surface 5a of the cylindrical body 5 with the portion bulging and enlarged. ) Is formed.

そして、この管状拡張流路機構(流路)4を形成する前記中央膨出体6の途中に段差部7を設けて、該流路4の流路幅mを大小に変化させて流動中の含泡液体を絞り作用を増大して内部の気泡の拡大を促進させている。即ち、上流側に比し、下流側を狭少にして気泡の延伸拡大を図っている。   A stepped portion 7 is provided in the middle of the central bulging body 6 forming the tubular expansion flow path mechanism (flow path) 4, and the flow path width m of the flow path 4 is changed to be larger or smaller. The squeezing action of the foam-containing liquid is increased to promote the expansion of the internal bubbles. That is, as compared with the upstream side, the downstream side is narrowed to expand and expand the bubbles.

また、図示しないが、間隙gで構成される流路4には同心環状の二以上の異径管を配設して分流させて泡の拡大を促す多層構成とすることもできる。   Moreover, although not shown in figure, the flow path 4 comprised by the gap | interval g can also be set as the multilayer structure which arrange | positions and distributes two or more concentric annular different diameter pipes, and promotes foam expansion.

8は中央膨出体6の下部に設けられる含泡液体の曲折凝集機構を示し、管状拡張流路機構4を経て来た含泡液体を前記中央膨出体6の中心軸O−Oの下流で集中凝集させるための含泡液体の曲折凝集機構8を構成している。この曲折凝集機構8により一旦拡大した気泡を有する含泡液体を集合させて、曲折される爾後の分離気化を促進させるための準備態勢状態を保持させることができる。   Reference numeral 8 denotes a bending and aggregating mechanism of the foam-containing liquid provided in the lower part of the central bulging body 6, and the foam-containing liquid that has passed through the tubular expansion channel mechanism 4 is downstream of the central axis OO of the central bulging body 6. The bending aggregation mechanism 8 of the foam-containing liquid for concentrating and coagulating is constituted. By this bending and aggregating mechanism 8, the bubble-containing liquid having bubbles that have once expanded can be gathered to maintain a ready state for promoting separation and vaporization after being bent.

10は、前記曲折凝集機構8の次段に形成される水平、平面状で扁平状の円周拡大拡散機構を示し、中心軸O−Oを中心にして直角の水平方向に延長した凝集された含泡液体を微少な間隔nを保持して円周状に拡大した気液分離用流路11を形成している。具体的には前記円筒体5の曲折凝集機構8より円周状に拡大する鍔部12と、この鍔部12と対抗して間隔nを備える拡張板部13を調節自在に対設して、前記鍔部12と拡張板部13とで形成される気液分離用流路11の開放端に気体と液体との分離排出口14を形成できるものである。   Reference numeral 10 denotes a horizontal, flat and flat circumferential expansion / diffusion mechanism formed in the next stage of the bending and aggregating mechanism 8, which is agglomerated in a horizontal direction perpendicular to the center axis OO. A gas-liquid separation channel 11 is formed by enlarging the bubble-containing liquid in a circumferential shape while maintaining a minute interval n. Specifically, a flange 12 that expands circumferentially from the bending and aggregating mechanism 8 of the cylindrical body 5 and an expansion plate 13 that has an interval n in opposition to the flange 12 are provided to be adjustable, A gas / liquid separation / discharge port 14 can be formed at the open end of the gas-liquid separation channel 11 formed by the flange portion 12 and the expansion plate portion 13.

15は、前記円筒体5と円周拡大拡散機構10を包囲する中空室であって、該中空室15の一部には含泡液体中の気泡分を排除する大気に通ずる排気管16を備え、また該中空室15の他方には脱泡された液体を貯溜保持できる液体貯溜部17を備える。なお、図において、18は液体貯溜部17の導出口、19は円周拡大拡散機構10の間隔nを微調節するための調節ビス、20は中央膨出体6の上端のインナースリーブ9を固定するビスである。   A hollow chamber 15 surrounds the cylindrical body 5 and the circumferential expansion / diffusion mechanism 10, and a part of the hollow chamber 15 is provided with an exhaust pipe 16 connected to the atmosphere for eliminating bubbles in the bubble-containing liquid. The other of the hollow chambers 15 is provided with a liquid reservoir 17 that can store and hold the defoamed liquid. In the figure, 18 is an outlet for the liquid reservoir 17, 19 is an adjustment screw for finely adjusting the interval n of the circumferential expansion / diffusion mechanism 10, and 20 is for fixing the inner sleeve 9 at the upper end of the central bulging body 6. It is a screw to do.

叙上の構成に基づいて作用を説明する。   The operation will be described based on the above configuration.

所望の含泡液体を、含泡液体加圧供給機構2を介して供給管1より含泡液体貯溜部3に供給する。ついで含泡液体は、円筒体5と中央膨出体6との間に形成される管状拡張流路機構4内に層状に導入され、液体中の気泡分は液体と共に細長に引張拡大し、曲折凝集機構8へ送給される。   A desired foam-containing liquid is supplied from the supply pipe 1 to the foam-containing liquid reservoir 3 via the foam-containing liquid pressurizing and supplying mechanism 2. Subsequently, the foam-containing liquid is introduced into the tubular expanded flow path mechanism 4 formed between the cylindrical body 5 and the central bulging body 6 in a layered manner, and bubbles in the liquid are stretched and elongated together with the liquid to bend. It is fed to the aggregation mechanism 8.

一旦拡大された気泡は、狭少な流路から開放された曲折凝集機構8内に溜まることにより容積は縮少するが、液体自体の伸長収縮が行われるために気泡の拡大縮少操作が活性状態となっている。   Once expanded, the volume is reduced by accumulating in the bending and aggregating mechanism 8 released from the narrow flow path, but the expansion and contraction operation of the bubble is active because the liquid itself is expanded and contracted. It has become.

引続き含泡液体は、平板状の気液分離用流路11に導入され、より一層薄層となり、円周方向への拡散拡大作用を受ける。そこで気泡は、矢符方向への拡散拡大作用を受けて、気泡は矢符方向への拡大拡開作用を受け、液体との分離作用が促進され、開口端の分離排出口14において完全に液体と分離した気体が気化して排出される。気体は排気管16によって外部に排気され、液体貯溜部17には脱気された液体のみが貯溜される。   Subsequently, the foam-containing liquid is introduced into the flat gas-liquid separation channel 11 to become a thinner layer, and is subjected to a diffusion expansion action in the circumferential direction. Therefore, the bubbles are subjected to a diffusion and expansion action in the direction of the arrow, and the bubbles are subjected to an expansion and expansion action in the direction of the arrow, and the separation action from the liquid is promoted, and the liquid is completely discharged at the separation outlet 14 at the opening end. The separated gas is vaporized and discharged. The gas is exhausted to the outside by the exhaust pipe 16, and only the degassed liquid is stored in the liquid storage portion 17.

この発明によれば、含泡液体中の気泡除去には、単に含泡液体に必要な圧力を付与し、含泡液体を管状流路及び平面状の拡大流路に供給させるだけで液中に含まれる気泡は拡大顕在化できるので、構成が簡単で、かつ各種装置への組込みも簡単にできるなどきわめて有益できる。   According to the present invention, for removing bubbles in the foam-containing liquid, simply applying the necessary pressure to the foam-containing liquid and supplying the foam-containing liquid to the tubular channel and the planar enlarged channel into the liquid. Since the contained bubbles can be enlarged and manifested, it is extremely beneficial because it is simple in construction and can be easily incorporated into various devices.

以上、本発明の一実施例を記述したが、図示では中心軸O−Oが垂直方向であるが、傾斜方向など好みの状態で実施できる。   Although one embodiment of the present invention has been described above, the central axis OO is in the vertical direction in the drawing, but can be implemented in a desired state such as an inclination direction.

管状拡張流路の構成の流路4は、円筒体5と中央膨出体6との間で形成される間隙gで形成されるが、段差部7で上流側と下流側との流路幅mを変化させているが、段差部7を省略して同一流路幅mとしたり、又は漸次と減少する可及的な流路幅mとして構成できる。   The flow path 4 having the configuration of the tubular expansion flow path is formed by a gap g formed between the cylindrical body 5 and the central bulging body 6, and the flow path width between the upstream side and the downstream side at the stepped portion 7. Although m is changed, the stepped portion 7 can be omitted to make the same flow path width m, or the flow path width m can be gradually reduced.

各種製造装置に対して脱泡を目的とする本発明は、途中いかなる工程でも実施できる。   The present invention aiming at defoaming with respect to various production apparatuses can be carried out in any process.

1 供給管
2 含泡液体加圧供給機構
3 含泡液体貯溜部
4 管状拡張流路機構(流路)
5 円筒体
5a 内周面
6 中央膨出体
6a 外周面
7 段差部
8 曲折凝集機構
9 インナースリーブ
10 円周拡大拡散機構
11 気液分離用流路
12 鍔部
13 拡張板部
14 分離排出口
15 中空室
16 排気管
17 液体貯溜部
18 導出口
19 調節ビス
20 ビス
n 間隔
m 流路幅
g 間隙
DESCRIPTION OF SYMBOLS 1 Supply pipe 2 Foam-containing liquid pressurization supply mechanism 3 Foam-containing liquid storage part 4 Tubular expansion flow path mechanism (flow path)
DESCRIPTION OF SYMBOLS 5 Cylindrical body 5a Inner peripheral surface 6 Central bulging body 6a Outer peripheral surface 7 Step part 8 Bending aggregation mechanism 9 Inner sleeve 10 Circumferential expansion diffusion mechanism 11 Gas-liquid separation flow path 12 Gutter part 13 Expansion board part 14 Separation discharge port 15 Hollow chamber 16 Exhaust pipe 17 Liquid reservoir 18 Outlet 19 Adjustment screw 20 Screw n Interval m Channel width g Gap

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 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 degassing method and apparatus for a bubble-containing liquid that eliminates bubbles mixed in various liquid materials including a viscous liquid material.

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 of using 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, the bubble which mixes or generate | occur | produces from a physical property, such as a density | concentration and an accuracy, has many problems on quality essentially, and it is inevitable to eliminate.

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。   Although it may be performed chemically using an antifoaming agent, it often has an adverse effect on the quality control of liquid products and is not general. 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 (see, for example, 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記載されている(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, Further, it is described that the liquid from which bubbles are removed is recovered (for example, see 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記載されている(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 described that bubbles in the liquid are taken out by decompression and the liquid from which the bubbles are removed is recovered (for example, see Patent Document 4).

特開2006−27012号公報JP 2006-27012 A 特開平10−43293号公報JP-A-10-43293 特開昭57−197004号公報JP 57-197004 A 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 both of Patent Documents 1 and 2 mentioned 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.

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。   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。   Further, the vacuum defoaming device of Patent Document 4 does not have a configuration in which the liquid flows in an annular shape in the liquid film forming nozzle.

本発明は、叙上の点に着目して成されたもので、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周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、排出後は減圧吸気機構を用いることなく大気圧下の排気機構で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提供することを目的とする。   The present invention has been made by paying attention to the above points, and allows the bubble-containing liquid that has been pressed and pressurized to pass through a circumferential tubular channel formed in one or more multi-annular tubular forms. Disperse the bubbles in the long and adjacent bubbles to the expanded state, and after agglomerating directly or in the center, the liquid is expanded horizontally and circumferentially with respect to the axis center. A bubble-containing liquid that effectively separates the air and air bubbles, and after discharge, removes the gas with an exhaust mechanism under atmospheric pressure without using a vacuum intake mechanism, and allows the degassed liquid to be removed. An object of the present invention is to provide a deaeration method and an apparatus therefor.

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円筒体の円筒体壁と前記円筒体内部に設けられた内装部材との間に形成される環管流路内で一層ないし多層の薄層となるように整流して流通させる環管整流工程、
加圧供給される含泡液体の前記環管流路の中心軸の下流に含泡液体を凝集させると共に水平方向に曲折させる曲折凝集工程、
含泡液体を薄層に形成して円周平面状に拡大して含泡液体中の隣り合う気泡を集合拡大して液体との分離を行わせるようにした気液分離工程、
液体中の気泡を取り出す大気圧下排気工程、
排気液体を集める液体採取工程、
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,
The bubble-containing liquid supplied under pressure is rectified so that it becomes one or more layers in an annular flow path formed between the cylindrical wall of the cylindrical body and the interior member provided inside the cylindrical body. collar rectification step be distributed to,
Bending aggregating step of bending in the horizontal direction together with coagulating foamed liquid downstream of the central axis of the collar passage foamed liquid to be supplied under pressure,
A gas-liquid separation step in which a foam-containing liquid is formed into a thin layer and expanded in a circumferential plane to collect and expand adjacent bubbles in the foam-containing liquid to separate them from the liquid,
An exhaust process under atmospheric pressure to extract bubbles in the liquid,
Liquid collection process for collecting exhaust liquid,
A degassing method for a foam-containing liquid, comprising:

(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円筒体の円筒体壁と、前記円筒体壁と間隙を介して形成されて内部に配設される内装部材との間の環管状の含泡液体の管状液路機構と、
含泡液体を前記内装部材の下部に集合させて水平方向に曲折させる曲折凝集機構と、
凝集された含泡液体を円周平面状に拡大させて含泡液体中の気泡を拡大させて、液体と分離できる円周拡大拡散機構と、
液体と分離した気泡を大気中に排気できる大気圧下排気機構と、
脱気液体を静止貯溜する機構と、
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;
An annular tubular foam-containing liquid between a cylindrical body wall for introducing a foam-containing liquid to be supplied under pressure and an interior member that is formed through the gap and disposed inside the cylindrical wall . a pipe-like fluid channel mechanism,
A bending and aggregating mechanism for collecting the foam-containing liquid at the lower part of the interior member and bending it in the horizontal direction;
A circumferentially expanding diffusion mechanism that expands the agglomerated foamed liquid in a circumferential plane to expand the bubbles in the foamed liquid, and can be separated from the liquid;
An atmospheric pressure exhaust mechanism capable of exhausting air bubbles separated from liquid into the atmosphere;
A mechanism for stationary storage of degassed liquid;
A degassing device for a foam-containing liquid, comprising:

(3)含泡液体の管状液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) said that the introduction of the tube-shaped liquid channel mechanism of bubble-containing liquid characterized by comprising providing a foamed liquid reservoir for introducing holding the foamed liquid (2) degassing of the bubble-containing liquid according apparatus.

(4)含泡液体の管状液路機構の間隙で形成される含泡液体の流路の大きさには、段差部を設けて上流側に対して下流側を小さくして狭搾り作用を増大できるようにして成ることを特徴とする前記(2)記載の含泡液体の脱気装置。 (4) The size of the flow path of the foamed liquid which is formed at the gap of the tube-shaped liquid channel mechanism of bubble-containing liquid, a narrow squeezing action to reduce the downstream side to the upstream side provided with a stepped portion The degassing device for a foam-containing liquid according to the above (2), characterized in that it can be increased.

(5)含泡液体の管状液路機構の間隙には、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)又は(4)記載の含泡液体の脱気装置。 (5) The gap between the tube-shaped liquid channel mechanism of bubble-containing liquid, wherein, characterized in that to not more by forming a flow path of a multilayer foamed liquid (2) or (4) foamed liquid according Deaeration device.

本発明に拠れば、含泡液体を加圧移送させる手段と、一層ないし多層の円管構成で流通路幅を細少して液体中の気泡を円周平面方向に拡大拡開させ凝集させること、並びに減圧吸引手段を用いないで含泡液体の加圧供給手段によって大気圧下に直接気化された気泡を排除できるので、食品中の風味や化粧品などの香料の脱気が無くなり、品質の向上が得られ、かつ構成が簡単で組立が容易であり、特に粘稠度の少ない含泡液体に有効であるなど、全体の構成が簡単に形成して消泡、脱泡を必要とする製造ラインに組み込むことができる。 According to the present invention, a means for pressurizing and transporting the foam-containing liquid, and the flow path width is narrowed by a single or multi-layered circular tube configuration to expand and expand the bubbles in the liquid in the circumferential plane direction, In addition, since the bubbles directly vaporized under atmospheric pressure can be eliminated by the pressure supply means of the foam-containing liquid without using the vacuum suction means, there is no degassing of flavors such as flavors and cosmetics in food, and the quality is improved. It is easy to assemble and easy to assemble, especially for foaming liquids with low viscosity. Can be incorporated.

本発明に係る脱泡装置の断面説明図Cross-sectional explanatory drawing of a defoaming apparatus according to the present invention 図1のII−II線断面図II-II sectional view of FIG. 図1のIII−III線断面図III-III 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.

以下に本発明の一実施例を図面と共に説明する。   An embodiment of the present invention will be described below with reference to the drawings.

1は含泡液体を加圧供給する含泡液体加圧供給機構2の供給管、3は含泡液体を導入保持する含泡液体貯溜部、4は前記含泡液体貯溜部3に続く環管状の含泡液体の管状流路機構を示し、中空状の円筒体5の上部には前記含泡液体貯溜部3が形成され、円筒体5の内部に配設される両端を固定して中央部分が膨出拡大した構成の内装部材に相当する中央膨出体6の外周面6aと円筒体5の内周面5aとの間に形成される間隙gにこの含泡液体の管状流路機構4(流路)が形成される。 Reference numeral 1 denotes a supply pipe of a foam-containing liquid pressurizing and supplying mechanism 2 that pressurizes and supplies the foam-containing liquid, 3 denotes a foam-containing liquid reservoir for introducing and holding the foam-containing liquid, and 4 denotes an annular tube following the foam-containing liquid reservoir 3. shows the foamed liquid in the tube-shaped flow channel mechanism, the upper portion of the hollow cylindrical body 5 the bubble-containing liquid storage portion 3 is formed, the center and both ends fixed to be disposed inside of the cylinder 5 pipe-shaped flow path of the bubble-containing liquid to the gap g formed between the portion and the inner peripheral surface 5a of the outer circumferential surface 6a and the cylindrical body 5 of the central bulging body 6 corresponding to the interior member of the bulging enlarged configuration A mechanism 4 (flow path) is formed.

そして、この管状流路機構(流路)4を形成する前記中央膨出体6の途中に段差部7を設けて、該流路4の流路幅mを大小に変化させて流動中の含泡液体を絞り作用を増大して内部の気泡の拡大を促進させている。即ち、上流側に比し、下流側を狭少にして気泡の延伸拡大を図っている。 Then, the provided step portion 7 in the middle of the central bulging body 6, in flowing the flow path width m of the flow path 4 is changed to a magnitude for forming a tube-shaped flow channel mechanism (passage) 4 The squeezing action of the foam-containing liquid is increased to promote the expansion of the internal bubbles. That is, as compared with the upstream side, the downstream side is narrowed to expand and expand the bubbles.

また、図示しないが、間隙gで構成される流路4には同心環状の二以上の異径管を配設して分流させて泡の拡大を促す多層構成とすることもできる。   Moreover, although not shown in figure, the flow path 4 comprised by the gap | interval g can also be set as the multilayer structure which arrange | positions and distributes two or more concentric annular different diameter pipes, and promotes foam expansion.

8は中央膨出体6の下部に設けられる含泡液体の曲折凝集機構を示し、管状流路機構4を経て来た含泡液体を前記中央膨出体6の中心軸O−Oの下流で集中凝集させるための含泡液体の曲折凝集機構8を構成している。この曲折凝集機構8により一旦拡大した気泡を有する含泡液体を集合させて、曲折される爾後の分離気化を促進させるための準備態勢状態を保持させることができる。 8 shows a bending aggregation mechanism foamed liquid provided in the lower portion of the central bulge body 6, downstream of the foamed liquid which came through a pipe-shaped flow path mechanism 4 of the center axis O-O of the central bulging body 6 The bending aggregation mechanism 8 of the foam-containing liquid for concentrating and coagulating is constituted. By this bending and aggregating mechanism 8, the bubble-containing liquid having bubbles that have once expanded can be gathered to maintain a ready state for promoting separation and vaporization after being bent.

10は、前記曲折凝集機構8の次段に形成される水平、平面状で扁平状の円周拡大拡散機構を示し、中心軸O−Oを中心にして直角の水平方向に延長した凝集された含泡液体を微少な間隔nを保持して円周状に拡大した気液分離用流路11を形成している。具体的には前記円筒体5の曲折凝集機構8より円周状に拡大する鍔部12と、この鍔部12と対抗して間隔nを備える拡張板部13を調節自在に対設して、前記鍔部12と拡張板部13とで形成される気液分離用流路11の開放端に気体と液体との分離排出口14を形成できるものである。   Reference numeral 10 denotes a horizontal, flat and flat circumferential expansion / diffusion mechanism formed in the next stage of the bending and aggregating mechanism 8, which is agglomerated in a horizontal direction perpendicular to the center axis OO. A gas-liquid separation channel 11 is formed by enlarging the bubble-containing liquid in a circumferential shape while maintaining a minute interval n. Specifically, a flange 12 that expands circumferentially from the bending and aggregating mechanism 8 of the cylindrical body 5 and an expansion plate 13 that has an interval n in opposition to the flange 12 are provided to be adjustable, A gas / liquid separation / discharge port 14 can be formed at the open end of the gas-liquid separation channel 11 formed by the flange portion 12 and the expansion plate portion 13.

15は、前記円筒体5と円周拡大拡散機構10を包囲する中空室であって、該中空室15の一部には含泡液体中の気泡分を排除する大気に通ずる排気管16を備え、また該中空室15の他方には脱泡された液体を貯溜保持できる液体貯溜部17を備える。なお、図において、18は液体貯溜部17の導出口、19は円周拡大拡散機構10の間隔nを微調節するための調節ビス、20は中央膨出体6の上端のインナースリーブ9を固定するビスである。   A hollow chamber 15 surrounds the cylindrical body 5 and the circumferential expansion / diffusion mechanism 10, and a part of the hollow chamber 15 is provided with an exhaust pipe 16 connected to the atmosphere for eliminating bubbles in the bubble-containing liquid. The other of the hollow chambers 15 is provided with a liquid reservoir 17 that can store and hold the defoamed liquid. In the figure, 18 is an outlet for the liquid reservoir 17, 19 is an adjustment screw for finely adjusting the interval n of the circumferential expansion / diffusion mechanism 10, and 20 is for fixing the inner sleeve 9 at the upper end of the central bulging body 6. It is a screw to do.

叙上の構成に基づいて作用を説明する。   The operation will be described based on the above configuration.

所望の含泡液体を、含泡液体加圧供給機構2を介して供給管1より含泡液体貯溜部3に供給する。ついで含泡液体は、円筒体5と中央膨出体6との間に形成される管状流路機構4内に層状に導入され、液体中の気泡分は液体と共に細長に引張拡大し、曲折凝集機構8へ送給される。 A desired foam-containing liquid is supplied from the supply pipe 1 to the foam-containing liquid reservoir 3 via the foam-containing liquid pressurizing and supplying mechanism 2. Then foamed liquid is introduced in layers formed in the tube-shaped flow channel mechanism 4 between the cylinder 5 and the central bulging body 6, the bubble content in the liquid will expand tensile elongated together with the liquid, bent It is fed to the aggregation mechanism 8.

一旦拡大された気泡は、狭少な流路から開放された曲折凝集機構8内に溜まることにより容積は縮少するが、液体自体の伸長収縮が行われるために気泡の拡大縮少操作が活性状態となっている。   Once expanded, the volume is reduced by accumulating in the bending and aggregating mechanism 8 released from the narrow flow path, but the expansion and contraction operation of the bubble is active because the liquid itself is expanded and contracted. It has become.

引続き含泡液体は、平板状の気液分離用流路11に導入され、より一層薄層となり、円周方向への拡散拡大作用を受ける。そこで気泡は、矢符方向への拡散拡大作用を受けて、気泡は矢符方向への拡大拡開作用を受け、液体との分離作用が促進され、開口端の分離排出口14において完全に液体と分離した気体が気化して排出される。気体は排気管16によって外部に排気され、液体貯溜部17には脱気された液体のみが貯溜される。   Subsequently, the foam-containing liquid is introduced into the flat gas-liquid separation channel 11 to become a thinner layer, and is subjected to a diffusion expansion action in the circumferential direction. Therefore, the bubbles are subjected to a diffusion and expansion action in the direction of the arrow, and the bubbles are subjected to an expansion and expansion action in the direction of the arrow, and the separation action from the liquid is promoted, and the liquid is completely discharged at the separation outlet 14 at the opening end. The separated gas is vaporized and discharged. The gas is exhausted to the outside by the exhaust pipe 16, and only the degassed liquid is stored in the liquid storage portion 17.

この発明によれば、含泡液体中の気泡除去には、単に含泡液体に必要な圧力を付与し、含泡液体を管状流路及び平面状の拡大流路に供給させるだけで液中に含まれる気泡は拡大顕在化できると共に、特に吸引手段を用いていないので、食品中の風味や化粧品などの香料の除去が無く、より品質の向上が期待され、かつ構成が簡単で、かつ各種装置への組込みも簡単にできるなどきわめて有益できる。 According to the present invention, for removing bubbles in the foam-containing liquid, simply applying the necessary pressure to the foam-containing liquid and supplying the foam-containing liquid to the tubular channel and the planar enlarged channel into the liquid. Bubbles contained can be enlarged and manifested, and since there is no particular use of suction means, there is no removal of flavors such as flavors and cosmetics in foods, higher quality is expected, the structure is simple, and various devices It can be extremely useful, such as easy integration into

以上、本発明の一実施例を記述したが、図示では中心軸O−Oが垂直方向であるが、傾斜方向など好みの状態で実施できる。   Although one embodiment of the present invention has been described above, the central axis OO is in the vertical direction in the drawing, but can be implemented in a desired state such as an inclination direction.

状流路の構成の流路4は、円筒体5と中央膨出体6との間で形成される間隙gで形成されるが、段差部7で上流側と下流側との流路幅mを変化させているが、段差部7を省略して同一流路幅mとしたり、又は漸次と減少する可及的な流路幅mとして構成できる。 A flow path 4 of the configuration of the pipe-shaped flow path is formed in the gap g formed between the cylinder 5 and the central bulging body 6, the channel width of the upstream side and the downstream side step part 7 Although m is changed, the stepped portion 7 can be omitted to make the same flow path width m, or the flow path width m can be gradually reduced.

各種製造装置に対して脱泡を目的とする本発明は、途中いかなる工程でも実施できる。   The present invention aiming at defoaming with respect to various production apparatuses can be carried out in any process.

1 供給管
2 含泡液体加圧供給機構
3 含泡液体貯溜部
4 管状流路機構(流路)
5 円筒体
5a 内周面
6 中央膨出体(内装部材)
6a 外周面
7 段差部
8 曲折凝集機構
9 インナースリーブ
10 円周拡大拡散機構
11 気液分離用流路
12 鍔部
13 拡張板部
14 分離排出口
15 中空室
16 排気管
17 液体貯溜部
18 導出口
19 調節ビス
20 ビス
n 間隔
m 流路幅
g 間隙
1 feed tube 2 foamed liquid pressure supply mechanism 3 foamed liquid storage portion 4 pipe-shaped flow channel mechanism (flow path)
5 Cylindrical body 5a Inner peripheral surface 6 Central bulging body (interior member)
6a Outer peripheral surface 7 Stepped portion 8 Bending and aggregating mechanism 9 Inner sleeve 10 Circumferential expansion and diffusion mechanism 11 Gas-liquid separation flow path 12 Gutter part 13 Expansion plate part 14 Separation discharge port 15 Hollow chamber 16 Exhaust pipe 17 Liquid storage part 18 Outlet port 19 adjusting screw 20 screw n interval m channel width g gap

(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円筒体の円筒体壁と前記円筒体内部に設けられた内装部材との間に形成される環管流路内で一層ないし多層の薄層となるように整流して流通させる環管整流工程、
加圧供給される含泡液体の前記環管流路の中心軸の下方に含泡液体を凝集させると共に水平方向に曲折させる曲折凝集工程、
含泡液体を薄層に形成して円周平面状に拡大して含泡液体中の隣り合う気泡を集合拡大して液体との分離を行わせるようにした気液分離工程、
液体中の気泡を取り出す大気圧下排気工程、
排気液体を集める液体採取工程、
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,
The bubble-containing liquid supplied under pressure is rectified so that it becomes one or more layers in an annular flow path formed between the cylindrical wall of the cylindrical body and the interior member provided inside the cylindrical body. Ring rectification process,
A bending agglomeration step of aggregating the foam-containing liquid below the central axis of the annular flow path of the foam-containing liquid to be supplied under pressure and bending it in the horizontal direction;
A gas-liquid separation step in which a foam-containing liquid is formed into a thin layer and expanded in a circumferential plane to collect and expand adjacent bubbles in the foam-containing liquid to separate them from the liquid,
An exhaust process under atmospheric pressure to extract bubbles in the liquid,
Liquid collection process for collecting exhaust liquid,
A degassing method for a foam-containing liquid, comprising:

8は中央膨出体6の下部に設けられる含泡液体の曲折凝集機構を示し、管状流路機構4を経て来た含泡液体を前記中央膨出体6の中心軸O−Oの下方で集中凝集させるための含泡液体の曲折凝集機構8を構成している。この曲折凝集機構8により一旦拡大した気泡を有する含泡液体を集合させて、曲折される爾後の分離気化を促進させるための準備態勢状態を保持させることができる。
Reference numeral 8 denotes a bending and aggregating mechanism of the foam-containing liquid provided at the lower part of the central bulging body 6. The foam-containing liquid that has passed through the tubular flow path mechanism 4 is placed below the central axis OO of the central bulging body 6. A bending aggregation mechanism 8 of the foam-containing liquid for concentrated aggregation is configured. By this bending and aggregating mechanism 8, the bubble-containing liquid having bubbles that have once expanded can be gathered to maintain a ready state for promoting separation and vaporization after being bent.

Claims (5)

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、
加圧供給される含泡液体の前記環管流路の中心軸の下流に含泡液体を凝集させると共に水平方向に曲折させる曲折凝集工程、
含泡液体を薄層に形成して円周平面状に拡大して含泡液体中の隣り合う気泡を集合拡大して液体との分離を行わせるようにした気液分離工程、
液体中の気泡を取り出す大気圧下排気工程、
排気液体を集める液体採取工程、
とより成ることを特徴とする含泡液体の脱気方法。
A foam-containing liquid pressurizing and supplying step for supplying foam-containing liquid under pressure,
A single-layer or multi-layer ring rectification process capable of thinly rectifying a bubble-containing liquid supplied under pressure into an annular shape;
A bending agglomeration step of aggregating the foamed liquid downstream of the central axis of the annular flow path of the foamed liquid supplied under pressure and bending it in the horizontal direction;
A gas-liquid separation step in which a foam-containing liquid is formed into a thin layer and expanded in a circumferential plane to collect and expand adjacent bubbles in the foam-containing liquid to separate them from the liquid,
An exhaust process under atmospheric pressure to extract bubbles in the liquid,
Liquid collection process for collecting exhaust liquid,
A degassing method for a foam-containing liquid, comprising:
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円筒体の円筒体壁と、間隙を介して形成されて内部に配設される中央膨出体との間の環管状の含泡液体の管状拡張液路機構と、
含泡液体を前記中央膨出体の中心軸の下流に集合させて水平方向に曲折させる曲折凝集機構と、
凝集された含泡液体を円周平面状に拡大させて含泡液体中の気泡を拡大させて、液体と分離できる円周拡大拡散機構と、
液体と分離した気泡を大気中に排気できる大気圧下排気機構と、
脱気液体を静止貯溜する機構と、
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;
Tubular expansion liquid of a ring-shaped foam-containing liquid between a cylindrical body wall for introducing a foam-containing liquid to be supplied under pressure and a central bulging body formed through a gap and disposed inside Road mechanism,
A bending and aggregating mechanism for collecting the foam-containing liquid downstream of the central axis of the central bulging body and bending it in the horizontal direction;
A circumferentially expanding diffusion mechanism that expands the agglomerated foamed liquid in a circumferential plane to expand the bubbles in the foamed liquid, and can be separated from the liquid;
An atmospheric pressure exhaust mechanism capable of exhausting air bubbles separated from liquid into the atmosphere;
A mechanism for stationary storage of degassed liquid;
A degassing device for a foam-containing liquid, comprising:
含泡液体の管状拡張液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。   The degassing device for a foam-containing liquid according to claim 2, wherein a foam-containing liquid reservoir for introducing and holding the foam-containing liquid is provided at the introduction portion of the tubular expanded liquid path mechanism for the foam-containing liquid. 含泡液体の管状拡張液路機構の間隙で形成される含泡液体の流路の大きさには、段差部を設けて上流側に対して下流側を小さくして狭搾り作用を増大できるようにして成ることを特徴とする請求項2記載の含泡液体の脱気装置。   The size of the flow path of the foam-containing liquid formed in the gap of the tubular expanded liquid channel mechanism of the foam-containing liquid can be increased by reducing the downstream side with respect to the upstream side by increasing the squeezing action. The degassing device for a foam-containing liquid according to claim 2, wherein 含泡液体の管状拡張液路機構の間隙には、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又は4記載の含泡液体の脱気装置。   5. A degassing device for foamed liquid according to claim 2 or 4, wherein a flow path of one or more foamed liquids is formed in the gap of the tubular expanded liquid path mechanism of the foamed liquid.
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