JP2000350929A - Two-part liquid mixing device - Google Patents

Two-part liquid mixing device

Info

Publication number
JP2000350929A
JP2000350929A JP11210197A JP21019799A JP2000350929A JP 2000350929 A JP2000350929 A JP 2000350929A JP 11210197 A JP11210197 A JP 11210197A JP 21019799 A JP21019799 A JP 21019799A JP 2000350929 A JP2000350929 A JP 2000350929A
Authority
JP
Japan
Prior art keywords
liquid
chamber
gas
mixed
mixing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
JP11210197A
Other languages
Japanese (ja)
Inventor
Shigeki Matsumoto
成樹 松本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NIPPON KANKYO CREATE KK
Original Assignee
NIPPON KANKYO CREATE KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NIPPON KANKYO CREATE KK filed Critical NIPPON KANKYO CREATE KK
Priority to JP11210197A priority Critical patent/JP2000350929A/en
Priority to PCT/JP2000/002221 priority patent/WO2000061268A1/en
Publication of JP2000350929A publication Critical patent/JP2000350929A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23123Diffusers consisting of rigid porous or perforated material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23126Diffusers characterised by the shape of the diffuser element
    • B01F23/231265Diffusers characterised by the shape of the diffuser element being tubes, tubular elements, cylindrical elements or set of tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23126Diffusers characterised by the shape of the diffuser element
    • B01F23/23127Screens, nets, grades or grids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/234Surface aerating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/234Surface aerating
    • B01F23/2341Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere
    • B01F23/23413Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere using nozzles for projecting the liquid into the gas atmosphere
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/45Mixing liquids with liquids; Emulsifying using flow mixing
    • B01F23/454Mixing liquids with liquids; Emulsifying using flow mixing by injecting a mixture of liquid and gas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/313Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
    • B01F25/3131Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/21Mixing gases with liquids by introducing liquids into gaseous media
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Nozzles (AREA)

Abstract

PROBLEM TO BE SOLVED: To highly efficiently mix and bring two liquids into contact with each other by intermingling super fine bubbles using a simple process. SOLUTION: In the two-part liquid mixing device which mixes a first liquid 11 with a second liquid 12, a liquid chamber for allowing passage of the first liquid 11, a gas chamber 3a positioned adjacently to the liquid chamber through a porous partition 6a, a means to supply a pressurized gas to the gas chamber 3a and a means 5 to atomize a second liquid 12 to the gas chamber 3a, are provided.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、液体と液体を混合
する二液混合装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a two-liquid mixing device for mixing a liquid and a liquid.

【0002】[0002]

【従来の技術】従来から、二液を混合するための装置と
して、固定容器内に回転撹拌機を有する混合機や、回転
容器を有する混合機、揺動振動機構を有する混合機、さ
らにこれらの混合機を組み合わせた混合機などがあり、
いかに均一に混合するか、いかに空気を含まないように
混合するか、逆に空気を含むように混合するか、いかに
経時変化のない混合液とするか、いかに二液の混合比の
調製を行うかなどさまざまな観点から改良や設計変更が
なされており、混合する液体に応じまた混合された液体
に応じた装置が考えられている。
2. Description of the Related Art Conventionally, as a device for mixing two liquids, a mixer having a rotary stirrer in a fixed container, a mixer having a rotary container, a mixer having an oscillating vibration mechanism, There are mixers that combine mixers, etc.
How to mix evenly, how to mix without air, how to mix to include air, how to make a mixed solution that does not change with time, how to adjust the mixing ratio of the two solutions Improvements and design changes have been made from various viewpoints such as the above, and devices corresponding to the liquid to be mixed and to the mixed liquid have been considered.

【0003】ところで、二液を混合する装置の中には単
に混合するだけではなく、二液間で反応を起こさせるよ
うなものや、二液間にさらに気体を接触させるもの、あ
るいは単に接触させるだけでなく気体側の物質を液体側
に移動させたり、逆に液体側の物質を気体側に移動させ
たりといった物質移動を伴ったものなどがある。たとえ
ば環境分野においては、深層曝気装置、水の塩素殺菌装
置、廃液処理装置などの環境装置に、食品工業において
は、炭酸水などの清涼飲料水の製造工程などに、石油化
学工業においては、酸化反応装置、水素添加反応装置な
どに広く液体と気体を混合接触させて、物質移動や化学
反応などを伴って混合を行わせる装置がある。
[0003] Incidentally, some devices for mixing two liquids do not merely mix, but also those that cause a reaction between the two liquids, those that further contact a gas between the two liquids, or those that simply contact the liquids. Not only that, there is a substance accompanied by mass transfer, such as moving a substance on the gas side to the liquid side, and conversely, moving a substance on the liquid side to the gas side. For example, in the environmental field, it is used for environmental equipment such as deep aeration equipment, chlorine disinfection equipment for water, and waste liquid treatment equipment; in the food industry, for the manufacturing process of soft drinks such as carbonated water; and in the petrochemical industry, it is used for oxidation. 2. Description of the Related Art There is an apparatus that mixes a liquid and a gas in a wide range with a reaction apparatus, a hydrogenation reaction apparatus, or the like, and performs mixing with mass transfer or chemical reaction.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、従来の
液体と気体との接触混合装置、たとえばエアレーション
タンクや静止型混合機においては、液体が大容量になる
と液体と液体、液体と気体の混合接触率が低くなり、ま
た回転撹拌機を有する装置では、混合接触率を上げるこ
とはある程度可能であるが電力費が高価となる問題があ
った。また気体を微細な噴霧とするノズルを使用した装
置では、ノズルの目詰まりや閉塞などのトラブルが発生
し、設備費及び保守管理費が高価となる問題があった。
However, in a conventional liquid / gas contact mixing apparatus such as an aeration tank or a static mixer, the mixing contact ratio of the liquid to the liquid and the liquid to the gas when the liquid has a large capacity. In a device having a rotary stirrer, the mixing contact ratio can be increased to some extent, but there is a problem in that the power cost is high. Further, in an apparatus using a nozzle that sprays fine gas, troubles such as clogging and clogging of the nozzle occur, and there is a problem that equipment costs and maintenance management costs are high.

【0005】本発明は、上述の点に鑑みてなされたもの
で、簡易な方法で、超微細気泡を混在させて二液を高効
率で混合接触させることができる二液混合装置を提供す
ることを課題とする。
The present invention has been made in view of the above points, and provides a two-liquid mixing apparatus capable of mixing and contacting two liquids with high efficiency by mixing ultra-fine bubbles by a simple method. As an issue.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
本発明の二液混合装置は、第一の液体と第二の液体を混
合する二液混合装置において、前記第一の液体を通過さ
せる液室と、該液室に多孔性の隔壁を介して隣接する気
室と、加圧された気体を前記気室に供給する手段と、前
記気室内に前記第二の液体を供給する手段とを備えてな
ることを特徴とするものである。
According to the present invention, there is provided a two-liquid mixing apparatus for mixing a first liquid and a second liquid, wherein the first liquid is passed through the two-liquid mixing apparatus. A liquid chamber, a gas chamber adjacent to the liquid chamber via a porous partition, means for supplying a pressurized gas to the gas chamber, and means for supplying the second liquid to the gas chamber. It is characterized by comprising.

【0007】この二液混合装置は、前記液室が曲面また
は平面を含む単面体または多面体で形成され、前記気室
が曲面または平面を含む単面体または多面体の前記隔壁
を介して該液室内に少なくとも一部が配されている形態
とすることができる。
In this two-liquid mixing apparatus, the liquid chamber is formed of a monohedron or a polyhedron having a curved surface or a flat surface, and the air chamber is inserted into the liquid chamber through the monohedral or polyhedral partition having a curved surface or a flat surface. At least a part thereof may be provided.

【0008】あるいは、液室と気室の関係を逆にして、
前記気室が曲面または平面を含む単面体または多面体で
形成され、前記液室が曲面または平面を含む単面体また
は多面体の前記隔壁を介して該気室内に少なくとも一部
が配されている形態とすることもできる。
Alternatively, the relationship between the liquid chamber and the air chamber is reversed,
A form in which the air chamber is formed of a monohedron or a polyhedron including a curved surface or a plane, and the liquid chamber is at least partially disposed in the air chamber via the partition of the monohedron or the polyhedron including the curved surface or the plane. You can also.

【0009】例えば、前記液室を円筒状または球面状に
形成し、前記気室を、円筒状または球面状に形成された
前記隔壁を介して該液室と同心円状に該液室内に少なく
とも一部が配されるようにしてもよいし、逆に、前記気
室を円筒状または球面状に形成し、前記液室を、円筒状
または球面状に形成された前記隔壁を介して該気室と同
心円状に該気室内に少なくとも一部が配されるようにし
てもよい。
For example, the liquid chamber is formed in a cylindrical or spherical shape, and at least one air chamber is formed in the liquid chamber concentrically with the liquid chamber through the partition formed in a cylindrical or spherical shape. May be arranged, or conversely, the air chamber is formed in a cylindrical or spherical shape, and the liquid chamber is formed through the partition formed in a cylindrical or spherical shape. At least a portion may be arranged concentrically in the air chamber.

【0010】また、前記隔壁を平板状あるいは曲板状ま
たはその組合せとし、前記液室と前記気室がその隔壁を
介して隣接する構成とすることもできる。
The partition may be in the form of a flat plate or a curved plate or a combination thereof, and the liquid chamber and the air chamber may be adjacent to each other via the partition.

【0011】「液室」は、第一の液体を通過させ得るも
のであれば、円筒形、直方形、球形、或いはそれらを組
み合わせた複合形等の種々の形状とすることができる。
これらの形状は、曲面または平面を含む単面体または多
面体と表現することができる。
The "liquid chamber" can have various shapes such as a cylindrical shape, a rectangular shape, a spherical shape, or a combined shape thereof, as long as it allows the first liquid to pass therethrough.
These shapes can be expressed as a monohedron or a polyhedron including a curved surface or a plane.

【0012】「気室」は、加圧された空気等の気体を受
容するものであれば、円筒形、直方形、球形、或いはそ
れらを組み合わせた複合形等の種々の形状とすることが
できる。これらの形状も、曲面または平面を含む単面体
または多面体と表現することができる。
The "air chamber" may have various shapes such as a cylindrical shape, a rectangular shape, a spherical shape, or a combined shape thereof as long as it can receive gas such as pressurized air. . These shapes can also be expressed as a monohedron or a polyhedron including a curved surface or a plane.

【0013】「液室」と「気室」との関係は、一方が他
方の内部にほぼ全部収容されるように配されていてもよ
いし、その一部のみが収容されるように配されていても
よい。
[0013] The relationship between the "liquid chamber" and the "air chamber" may be such that one is accommodated substantially entirely in the other, or only a part thereof is accommodated. May be.

【0014】「第二の液体を供給する」とは、第二の液
体が、液状である場合だけではなく微粒子として噴霧さ
れる場合も含むものとする。
"Supplying the second liquid" includes not only the case where the second liquid is liquid but also the case where the second liquid is sprayed as fine particles.

【0015】「第一の液体」は、たとえば工場からの排
水、下水道からの処理水や汚泥、プール用水、魚養殖用
水、観賞魚用水槽水などの水、あるいは食品工場におけ
る清涼飲料水や調味料などの原料、石油化学工業におけ
る原料となる物質など、流動性がある液体であれば粘度
が高いものであっても固形物を含んでいるものであって
もよい。「第二の液体」は、第一の液体と混合あるいは
反応させる液体を意味し、たとえば水、ハロゲン、酸、
アルカリ、フェノール、クレオソート、希塩酸、希硫酸
などの、希釈剤、殺菌剤や酸化剤、還元剤、添加剤、着
色剤、漂白剤、乳化剤、湿潤剤、分散剤などノズルから
供給できる液体であれば特に限定されるものではない。
「第一の液体」と「第二の液体」はともに液体である
が、混合する液体のうち、より体積の多い方を第一の液
体に少ない方を第二の液体に、あるいは粘度の高い方を
第一の液体に低い方を第二の液体に選択する方が、装置
を稼動させる上での電力費などの経済的観点からまた保
守管理上も望ましい。
The "first liquid" is, for example, wastewater from factories, treated water or sludge from sewers, water for pools, water for fish culture, aquarium water for ornamental fish, or soft drinks or seasonings in food factories. Liquids having a high viscosity or solids may be used as long as they are fluid liquids, such as raw materials such as raw materials and materials used as raw materials in the petrochemical industry. "Second liquid" means a liquid that is mixed or reacted with a first liquid, such as water, halogen, acid,
Liquids such as alkali, phenol, creosote, dilute hydrochloric acid, dilute sulfuric acid, etc. which can be supplied from nozzles such as diluents, disinfectants, oxidizing agents, reducing agents, additives, coloring agents, bleaching agents, emulsifiers, wetting agents, dispersants, etc. It is not particularly limited.
The "first liquid" and the "second liquid" are both liquids, but of the liquids to be mixed, the larger liquid is the first liquid and the smaller liquid is the second liquid, or the liquid has a higher viscosity. It is more desirable to select the first liquid as the first liquid and the second liquid as the second liquid from an economic viewpoint such as power cost for operating the apparatus and also from the viewpoint of maintenance.

【0016】「気体」とは、たとえば空気、酸素、炭酸
ガス、塩素ガス、窒素、水素などで上記液体中に混在さ
せたり反応させたりあるいは液体中の物質を吸収したり
するような目的で使用されるものであれば特に限定され
るものではない。
The term "gas" is used for the purpose of mixing with or reacting with the above liquid or absorbing substances in the liquid with, for example, air, oxygen, carbon dioxide, chlorine gas, nitrogen or hydrogen. It is not particularly limited as long as it is performed.

【0017】「同心円状」とは、中心或いは中心軸が完
全に一致している必要はなく、多少の位置ずれをした場
合も含むものとする。
The term "concentric" does not require that the centers or center axes be completely coincident with each other, and includes a case where the positions are slightly shifted.

【0018】「円筒状」とは、必ずしも完全な円筒形で
ある必要はなく、多少の凹凸、或いは変形があったとし
ても、全体として円筒形である場合も含むものとする。
The term "cylindrical" does not necessarily mean a perfect cylindrical shape, but includes a cylindrical shape as a whole, even if there are some irregularities or deformations.

【0019】「球面状」とは、必ずしも完全な球形であ
る必要はなく、異なる曲率半径を有する複数の曲面から
構成される形状も含むものとする。
The term "spherical" does not necessarily mean a perfect spherical shape, but includes a shape composed of a plurality of curved surfaces having different radii of curvature.

【0020】「平板状」とは、必ずしも完全な平面であ
る必要はなく、多少の凹凸、或いは変形があったとして
も、全体として平板形である場合も含むものとする。
The term "flat" does not necessarily mean a perfect flat surface, and includes a flat plate as a whole, even if there are some irregularities or deformations.

【0021】「混合液」とは、第一の液体と第二の液体
と気体とが混合された液を意味し、仮に反応を伴うよう
な混合であっても、混合されていれば反応途中であるか
反応後であるかを問うものではない。
The term "mixed liquid" refers to a liquid in which a first liquid, a second liquid, and a gas are mixed. It doesn't matter if it is after or after the reaction.

【0022】「流出口」とは、本発明の二液混合装置で
作られた混合液が装置から排出される口を意味し、外管
の一端に有していればこの流出口がさらに他の装置や管
に接続されていてもよい。
The term "outlet" means an outlet from which a mixed liquid produced by the two-liquid mixing apparatus of the present invention is discharged from the apparatus. May be connected to the device or pipe.

【0023】「液体供給口」とは第一の液体が供給され
る外管の一部に設けられた供給口を意味し、その大きさ
は第一の液体がスムーズに供給できれば特に限定される
ものではないが、液体供給口の位置は第一の液体と第二
の液体と気体とが混合される時間を考慮して、流出口と
は反対側に設けることが好ましい。もっとも流出口を管
に連結して他の装置に接続したり、あるいは第一の液体
と第二の液体の性質からそのような時間を考慮する必要
がないときには供給口が流出口の多少近くに設けられて
いてもよい。また液体供給口は連続して液体を供給する
ことができる構成としても、液体を供給した後供給口が
閉じる構成としても、あるいは供給量が調整できる調整
弁を有するような構成としてもよい。
"Liquid supply port" means a supply port provided in a part of the outer tube to which the first liquid is supplied, and its size is particularly limited as long as the first liquid can be supplied smoothly. Although not intended, the position of the liquid supply port is preferably provided on the side opposite to the outlet in consideration of the time during which the first liquid, the second liquid, and the gas are mixed. However, when it is not necessary to connect the outlet to a pipe and connect it to another device, or when such time does not need to be considered due to the properties of the first liquid and the second liquid, the supply port is located slightly closer to the outlet. It may be provided. Further, the liquid supply port may be configured to be able to continuously supply the liquid, may be configured to close the supply port after supplying the liquid, or may be configured to have an adjustment valve capable of adjusting the supply amount.

【0024】「外管」は、混合液の流出口と液体供給口
を有している管であれば、特にその大きさは限定される
ものではなく、たとえば第一の液体が排水のように多量
であればその長さも径も数メートルのものに、また観賞
用魚水槽水であれば数十センチのものにと状況に応じて
対応すればよい。また外管の内側には、第一の液体が逆
流しないようにするための仕切板や羽根を設けてもよ
い。
The "outer pipe" is not particularly limited in size as long as it has a mixed liquid outlet and a liquid supply port. Depending on the situation, the length and diameter may be several meters if the amount is large, and several tens of centimeters may be used for ornamental fish tank water. Further, a partition plate or a blade for preventing the first liquid from flowing backward may be provided inside the outer tube.

【0025】「内管」は、外管の流出口側の端部に多孔
性の気体排出口を有し、かつ混合前の気体が供給される
気体供給口を一部に有して、上記外管との間で空間を形
成するように外管の中に同心状に配されものであるが、
外管と内管の間に形成された空間に第一の液体が流動で
きれば、必ずしも完全な同心状である必要はない。「外
管の流出口側の端部に多孔性の気体排出口を有し」と
は、気体排出口が、必ずしも外管の流出口側近傍に設け
られていることを意味するものではない。また、この多
孔性の気体排出口が外管の流出口側の端部に設けられて
おり、内管の気体排出口が外管に設けられた液体供給口
よりも液体流動方向に対して下流であれば、必ずしも内
管全体が外管の内部に設けられている必要はない。
The “inner pipe” has a porous gas discharge port at the end of the outer pipe on the outflow side, and has a gas supply port to which gas before mixing is supplied in part. It is arranged concentrically inside the outer tube so as to form a space with the outer tube,
If the first liquid can flow into the space formed between the outer tube and the inner tube, the first liquid need not necessarily be completely concentric. “Having a porous gas outlet at the end of the outer tube on the outlet side” does not mean that the gas outlet is necessarily provided near the outlet of the outer tube. Also, this porous gas outlet is provided at the end of the outer tube on the outlet side, and the gas outlet of the inner tube is located downstream of the liquid supply port provided in the outer tube in the liquid flow direction. If so, the entire inner pipe does not necessarily need to be provided inside the outer pipe.

【0026】「気体排出口」は多孔性であればよいが、
その長さや径は以下のような点を考慮して調整すること
が好ましい。すなわちノズルから供給された第二の液体
が内管の先端部に溜まるような状態では、微細な粒子と
して第二の液体をすべての多孔から均一に排出すること
が難しくなるため、供給され多孔に付着した第二の液体
を気体の圧力によって均一に排出することができるよう
に、気体の流速や気体排出口の長さや径を決定すること
が望ましい。たとえば、時間当たりの気体の流量やノズ
ルから供給される第二の液体量や多孔部分の内面積を考
慮して、第二の液体の混合が多いような系では気体排出
口の長さを長くしたり径を大きくしたり、逆に第二の液
体の混合が少ないような系では気体排出口の径を小さく
するなどの調整をすることが好ましい。
The "gas outlet" may be porous,
The length and diameter are preferably adjusted in consideration of the following points. In other words, in a state where the second liquid supplied from the nozzle accumulates at the tip of the inner tube, it becomes difficult to uniformly discharge the second liquid from all the pores as fine particles, so that the supplied liquid becomes porous. It is desirable to determine the flow rate of the gas and the length and diameter of the gas discharge port so that the attached second liquid can be uniformly discharged by the pressure of the gas. For example, in consideration of the gas flow rate per hour, the amount of the second liquid supplied from the nozzle, and the inner area of the porous portion, the length of the gas outlet is increased in a system in which the second liquid is frequently mixed. In a system in which the mixing of the second liquid is small or the diameter of the gas discharge port is small, it is preferable to make adjustments such as reducing the diameter of the gas discharge port.

【0027】「多孔性」とは、内部または表面に多数の
小さな外部に通ずる孔状、あるいは気泡状の空隙をもつ
もので、気体を微細に排出できかつ通過する第二の液体
や気体、外側を通過する第一の液体によって損壊をうけ
るようなものでなければ特に限定されるものではない。
たとえばPVA(ポリビニルアルコール)、PVC(ポ
リ塩化ビニル)、ポリウレタンなどのプラスチックを材
質とする多孔性プラスチックや多孔性金属あるいは多孔
性セラミックを、排出される気体の量や第二の液体の量
に応じて用いることができる。また「気体供給口」は気
体を供給した後供給口が閉じる構成としても、あるいは
供給量が調整できる調整弁を有するような構成としても
よい。
The term "porous" refers to a substance having a large number of small pores or bubbles inside or on the inside or on the surface, which can discharge gas finely and pass through the second liquid or gas. There is no particular limitation as long as it is not damaged by the first liquid passing through.
For example, a porous plastic or a porous metal or a ceramic made of plastic such as PVA (polyvinyl alcohol), PVC (polyvinyl chloride), or polyurethane may be used in accordance with the amount of gas discharged or the amount of the second liquid. Can be used. The “gas supply port” may be configured to close the supply port after supplying the gas, or may be configured to include an adjustment valve capable of adjusting the supply amount.

【0028】「第二の液体用供給管」は、内管内側の気
体排出口近傍に混合前の第二の液体を供給するノズルを
一端に、混合前の前記第二の液体が供給される液体供給
口を他端に有するもので、第一の液体や気体と同様、第
二の液体の性質や目的に応じて適当な長さ、径とするこ
とが可能である。第二の液体用供給管は、ノズルから第
二の液体が内管内側に均等に供給できるように内管の同
心状に配されることが好ましい。「ノズル」は第二の液
体を高速度で供給できるものであれば、特にその形状は
限定されるものではないが、内管内側の気体排出口近傍
全体に均一に効率よく第二の液体を供給できるものであ
ることが望ましい。そのように均一に効率よく第二の液
体を供給できるノズルであれば、ノズルの全面から供給
するものであっても、側面からのみ供給するものであっ
てもよい。
The "second liquid supply pipe" has a nozzle for supplying the second liquid before mixing near the gas discharge port inside the inner pipe, and the second liquid before mixing is supplied at one end. It has a liquid supply port at the other end, and can have an appropriate length and diameter according to the properties and purpose of the second liquid, like the first liquid or gas. The second liquid supply pipe is preferably arranged concentrically with the inner pipe so that the second liquid can be evenly supplied from the nozzle to the inside of the inner pipe. The shape of the “nozzle” is not particularly limited as long as it can supply the second liquid at a high speed, but the second liquid is uniformly and efficiently supplied to the entire vicinity of the gas outlet inside the inner tube. It is desirable that it can be supplied. As long as the nozzle can supply the second liquid uniformly and efficiently, the nozzle may be supplied from the entire surface of the nozzle or may be supplied only from the side surface.

【0029】[0029]

【発明の実施の形態】以下、図面を参照して本発明の一
実施の形態による二液混合装置について説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a two-liquid mixing apparatus according to an embodiment of the present invention will be described with reference to the drawings.

【0030】図1は本発明の一実施の形態による二液混
合装置の概略構成を示す断面図である。
FIG. 1 is a sectional view showing a schematic configuration of a two-liquid mixing apparatus according to one embodiment of the present invention.

【0031】本発明の一実施の形態による二液混合装置
1は、第一の液体としての汚泥11を供給する液体供給
口7を側部に有する外管または液室2と、外管2との間
で空間を形成するように外管2の中に同心状に配された
内管または気室3と、内管3の内部に同心円状に配され
た第二の液体用供給管4とを有した構成となっている。
The two-liquid mixing apparatus 1 according to one embodiment of the present invention comprises an outer tube or liquid chamber 2 having a liquid supply port 7 for supplying sludge 11 as a first liquid on the side, An inner tube or air chamber 3 concentrically arranged in the outer tube 2 so as to form a space therebetween, and a second liquid supply tube 4 concentrically arranged in the inner tube 3. Is provided.

【0032】外管2は、汚泥11と、第二の液体として
の35%の過酸化水素12と、気体としての空気13と
が混合された混合液14を流出する流出口10を液体流
動方向の下流に有している。内管3は多孔性の気体排出
口6または多孔性の隔壁6を外管2の流出口10側の端
部に有し、空気13が供給される気体供給口8を側部に
有している。加圧された空気13を内管3に供給する手
段、例えばポンプ、圧縮機や関連の配管など(図示せ
ず)が気体供給口8に連結されている。気体排出口6
は、外管2の液体供給口7よりも液体流動方向に対し下
流であって、外管2のほぼ中央に位置し、側面のみが多
孔質のPVCで構成されている。第二の液体用供給管4
は内管3の内側の気体排出口6の近傍に過酸化水素12
を噴霧するノズル(供給手段)5を一端に有し、過酸化
水素12を供給する液体供給口9を他端に有している。
The outer pipe 2 is connected to an outlet 10 for flowing out a mixed liquid 14 in which sludge 11, 35% hydrogen peroxide 12 as a second liquid, and air 13 as a gas are mixed. Downstream. The inner pipe 3 has a porous gas discharge port 6 or a porous partition wall 6 at the end of the outer pipe 2 on the outlet 10 side, and has a gas supply port 8 to which air 13 is supplied on a side. I have. A means for supplying the pressurized air 13 to the inner pipe 3, for example, a pump, a compressor and related piping (not shown) is connected to the gas supply port 8. Gas outlet 6
Is located downstream of the liquid supply port 7 of the outer tube 2 in the liquid flow direction and is located substantially at the center of the outer tube 2, and only the side surfaces are made of porous PVC. Second liquid supply pipe 4
Is located near the gas outlet 6 inside the inner pipe 3.
Has a nozzle (supply means) 5 at one end and a liquid supply port 9 for supplying hydrogen peroxide 12 at the other end.

【0033】次に、本発明の一実施の形態による二液混
合装置を使用した汚泥11の処理を例にとって説明す
る。汚泥11は完全な液体ではないが、このような粘性
の高い物質であっても容易に混合が可能である。
Next, the treatment of sludge 11 using the two-liquid mixing apparatus according to one embodiment of the present invention will be described as an example. Although the sludge 11 is not a perfect liquid, it can be easily mixed even with such a highly viscous substance.

【0034】先ず、汚泥(第一の液体)11を外管2内
へ第一の液体用供給口7から供給する。空気(気体)1
3は気体供給口8から内管3内へ供給され、過酸化水素
(第二の液体)12は第二の液体供給口9から第二の液
体用供給管4内に供給され、続いて第二の液体用供給管
4の先端に設けられたノズル5から過酸化水素12が内
管3の多孔性の気体排出口6の内側に噴霧される。一
方、汚泥11は少しずつ外管2の液体流動方向に対し下
流へと移動し、それとともに多孔性の気体排出口6の内
側に付着している過酸化水素12が、空気13とともに
多孔性の気体排出口6から外管2の内部へ排出される。
排出された過酸化水素12と空気13は微細な粒子とな
って汚泥11中に混合される。混合された汚泥11、過
酸化水素12、空気13は後から続いて供給されてくる
汚泥11などによって、外管2の流出口10から混合さ
れて流出される。第一の液体用供給口7から供給された
混合前の汚泥11のMLSS(曝気槽内固形物)は50
00〜8000ppmであるが、混合液14では100
0〜2000ppmであり、分解反応が微細粒子となっ
て混合された過酸化水素によって効果的に行われたこと
が確認できる。
First, sludge (first liquid) 11 is supplied into the outer pipe 2 from the first liquid supply port 7. Air (gas) 1
3 is supplied from the gas supply port 8 into the inner pipe 3, and hydrogen peroxide (second liquid) 12 is supplied from the second liquid supply port 9 into the second liquid supply pipe 4. Hydrogen peroxide 12 is sprayed from the nozzle 5 provided at the tip of the second liquid supply pipe 4 into the inside of the porous gas discharge port 6 of the inner pipe 3. On the other hand, the sludge 11 gradually moves downstream with respect to the liquid flow direction of the outer pipe 2, and the hydrogen peroxide 12 adhering to the inside of the porous gas discharge port 6 becomes The gas is discharged from the gas discharge port 6 into the outer tube 2.
The discharged hydrogen peroxide 12 and air 13 are mixed into sludge 11 as fine particles. The mixed sludge 11, hydrogen peroxide 12, and air 13 are mixed and discharged from the outlet 10 of the outer pipe 2 by the sludge 11 supplied subsequently and the like. The MLSS (solids in the aeration tank) of the sludge 11 before mixing supplied from the first liquid supply port 7 is 50
100 to 8000 ppm, but 100
It is 0 to 2000 ppm, and it can be confirmed that the decomposition reaction was effectively performed by the hydrogen peroxide mixed as fine particles.

【0035】図2は本発明の他の実施の形態による二液
混合装置の概略構成を示す断面図である。
FIG. 2 is a sectional view showing a schematic configuration of a two-liquid mixing apparatus according to another embodiment of the present invention.

【0036】図2の二液混合装置1aの構成は次のよう
である。第一の液体11を通過させる液室2aと、該液
室2aに多孔性の隔壁6aを介して隣接する気室3a
と、加圧された気体13を気室3aに供給する圧縮機な
どの手段と、気室3a内に第二の液体12を噴霧する単
数または複数(図2では2個)の手段5、例えば噴霧ノ
ズル5などを備えている。液室2aは、第一の液体11
と、第二の液体12と、気体としての空気13とが混合
された混合液14を流出する流出口10aを液体流動方
向の下流に有している。気室3aは多孔性の平板状隔壁
6aにより液室2aと連通している。また、気室3aは
気体13が供給される気体供給口8aを側部に有してい
る。第二の液体用供給管4aが気室3aの側部に設けら
れ、この先端に第二の液体12を噴霧する手段5が取り
付けられている。
The structure of the two-liquid mixing device 1a shown in FIG. 2 is as follows. A liquid chamber 2a through which the first liquid 11 passes, and an air chamber 3a adjacent to the liquid chamber 2a via a porous partition wall 6a.
A means such as a compressor for supplying the pressurized gas 13 to the gas chamber 3a, and one or more (two in FIG. 2) means 5 for spraying the second liquid 12 into the gas chamber 3a, for example. A spray nozzle 5 and the like are provided. The liquid chamber 2a contains the first liquid 11
And an outlet 10a for flowing out a mixed liquid 14 in which a second liquid 12 and air 13 as a gas are mixed, is provided downstream in the liquid flowing direction. The air chamber 3a communicates with the liquid chamber 2a by a porous flat partition wall 6a. The gas chamber 3a has a gas supply port 8a to which the gas 13 is supplied on a side portion. A second liquid supply pipe 4a is provided on the side of the air chamber 3a, and a means 5 for spraying the second liquid 12 is attached to a tip of the second liquid supply pipe 4a.

【0037】この二液混合装置1aにより混合液14は
次のように製造される。先ず、第一の液体11を液室2
a内へ第一の液体用供給口7aから供給する。気体13
は気体供給口8aから気室3a内へ供給される。第二の
液体12は第二の液体用供給管4a内に供給され、続い
てノズル5から気室3a内に噴霧される。一方、第一の
液体11は少しずつ液室2aの液体流動方向に移動し、
それとともに隔壁6aに付着している第二の液体12
が、気体13とともに多孔性の隔壁6aから液室2a内
へ排出される。排出された液体12と気体13は微細な
粒子となって第一の液体11中に混合されて泡状(図に
多数の小粒子として示す)となる。混合された第一の液
体11、第二の液体12、気体13は後から続いて供給
されてくる第一の液体11などによって、液室2aの流
出口10aから混合液14として流出される。
The mixed liquid 14 is manufactured by the two-liquid mixing apparatus 1a as follows. First, the first liquid 11 is supplied to the liquid chamber 2.
a from the first liquid supply port 7a. Gas 13
Is supplied from the gas supply port 8a into the air chamber 3a. The second liquid 12 is supplied into the second liquid supply pipe 4a, and is subsequently sprayed from the nozzle 5 into the air chamber 3a. On the other hand, the first liquid 11 gradually moves in the liquid flowing direction of the liquid chamber 2a,
At the same time, the second liquid 12 adhered to the partition 6a
Is discharged from the porous partition wall 6a together with the gas 13 into the liquid chamber 2a. The discharged liquid 12 and gas 13 become fine particles and are mixed into the first liquid 11 to form a foam (shown as many small particles in the figure). The mixed first liquid 11, second liquid 12, and gas 13 are discharged as a mixed liquid 14 from the outlet 10a of the liquid chamber 2a by the first liquid 11 and the like that are subsequently supplied.

【0038】図2では液室2aが気室3aの上に重ねら
れているが、逆に気室3aを液室2aの上に重ねるよう
に構成してもよい。また、液室2aおよび気室3aの横
断面はマッチ箱のような矩形でも半円形でもよい。
Although the liquid chamber 2a is overlaid on the gas chamber 3a in FIG. 2, the gas chamber 3a may be overlaid on the liquid chamber 2a. Further, the cross sections of the liquid chamber 2a and the air chamber 3a may be rectangular or semicircular like a match box.

【0039】図3は本発明の他の実施の形態による二液
混合装置の概略構成を示す断面図である。
FIG. 3 is a sectional view showing a schematic configuration of a two-liquid mixing apparatus according to another embodiment of the present invention.

【0040】図3の二液混合装置1bの構成は次のよう
である。第一の液体11を通過させる中央が膨れた略円
筒状の液室2bが縦方向に配置され、該液室2bの中を
横方向に円筒状の気室3bが配置されている。液室2b
の一端に第一の液体用供給口7bが設けられている。気
室3bは多孔性の円筒状隔壁6bにより囲繞され、液室
2bと気室3bとはこの多孔性の円筒状隔壁6bを介し
て隣接している。すなわち、気室3bは多孔性の隔壁6
bにより液室2bと連通している。気室3bは加圧され
た気体13を気室3bに供給する気体供給口8bを備え
ている。気室3b内に第二の液体12を噴霧する手段
5、例えば噴霧ノズルなどを備えている。液室2bは、
第一の液体11と、第二の液体12と、気体13とが混
合された混合液14を流出する流出口10bを液体流動
方向の下流端に有している。また、気室3bは気体13
が供給される気体供給口8bを側部に有し、第二の液体
12を供給する管4bが気室3bの側部に設けられ、こ
の先端に第二の液体12を噴霧する手段5が取り付けら
れている。二液混合装置1bにより混合液14を製造す
る方法は上記の実施の形態における説明に類似するので
これに代替し、詳細な説明は省略する。図3の実施の形
態では、液室2bを縦方向に配置し、気室3bを横方向
に配置するように説明したが、これらを逆配置にするこ
とも90度傾けた配置にすることもできる。
The structure of the two-liquid mixing device 1b shown in FIG. 3 is as follows. A substantially cylindrical liquid chamber 2b whose center is swollen and through which the first liquid 11 passes is vertically arranged, and a cylindrical air chamber 3b is horizontally arranged inside the liquid chamber 2b. Liquid chamber 2b
Is provided with a first liquid supply port 7b at one end. The air chamber 3b is surrounded by a porous cylindrical partition 6b, and the liquid chamber 2b and the air chamber 3b are adjacent to each other via the porous cylindrical partition 6b. That is, the air chamber 3 b is formed of the porous partition wall 6.
b communicates with the liquid chamber 2b. The gas chamber 3b has a gas supply port 8b for supplying the pressurized gas 13 to the gas chamber 3b. A means 5 for spraying the second liquid 12 into the air chamber 3b, for example, a spray nozzle is provided. The liquid chamber 2b is
An outlet 10b for flowing out a mixed liquid 14 in which the first liquid 11, the second liquid 12, and the gas 13 are mixed is provided at a downstream end in the liquid flowing direction. The air chamber 3b is a gas 13
Is provided on the side of the gas chamber 3b, and a means 5 for spraying the second liquid 12 at the tip of the pipe 4b for supplying the second liquid 12 is provided. Installed. The method for producing the mixed liquid 14 by the two-liquid mixing device 1b is similar to the description in the above-described embodiment, and therefore is replaced with this and the detailed description is omitted. In the embodiment of FIG. 3, the liquid chamber 2b is arranged in the vertical direction, and the gas chamber 3b is arranged in the horizontal direction. However, these may be arranged reversely or at an angle of 90 degrees. it can.

【0041】図4は本発明のさらに異なる実施の形態に
よる二液混合装置の概略構成を示す断面図である。
FIG. 4 is a sectional view showing a schematic configuration of a two-liquid mixing apparatus according to still another embodiment of the present invention.

【0042】図4の二液混合装置1cの構成は次のよう
である。第一の液体11を通過させる円筒状の液室2c
が横方向に配置され、該液室2cの周囲を円筒状の気室
3cが囲繞している。液室2cに第一の液体用供給口7
cが設けられている。気室3cは多孔性の円筒状隔壁6
cにより囲繞され、液室2cと気室3cとは多孔性の円
筒状隔壁6cを介して隣接している。すなわち、気室3
cは多孔性の隔壁6cを通して液室2cと連通してい
る。気室3cは加圧された気体13を供給する気体供給
口8cを備え、気室3c内に第二の液体用供給管4cと
その先端に固定された第二の液体12を噴霧する手段
5、例えば噴霧ノズルを備えている。液室2cは、第一
の液体11と、第二の液体12と、気体13とが混合さ
れた混合液14を流出する流出口10cを液体流動方向
の下流に有している。二液混合装置1cにより混合液1
4を製造する方法は上記の実施の形態に類似するのでこ
れに代替し、その詳細な説明は省略する。図4の実施の
形態では、液室2cと気室3cとが同心円状に横方向に
配置されているが、縦方向に配置してもよい。また、液
室2cと気室3cとの配置を逆にしてもよい。即ち、気
室3cは液室2cの内側に配置されるようにしてもよ
い。
The structure of the two-liquid mixing device 1c shown in FIG. 4 is as follows. Cylindrical liquid chamber 2c through which first liquid 11 passes
Are arranged in the lateral direction, and a cylindrical air chamber 3c surrounds the liquid chamber 2c. The first liquid supply port 7 is provided in the liquid chamber 2c.
c is provided. The air chamber 3 c has a porous cylindrical partition wall 6.
c, and the liquid chamber 2c and the air chamber 3c are adjacent to each other via a porous cylindrical partition wall 6c. That is, the air chamber 3
c communicates with the liquid chamber 2c through the porous partition 6c. The gas chamber 3c is provided with a gas supply port 8c for supplying a pressurized gas 13, and means 5 for spraying the second liquid supply pipe 4c and the second liquid 12 fixed at the tip thereof into the gas chamber 3c. For example, a spray nozzle is provided. The liquid chamber 2c has an outlet 10c for flowing out a mixed liquid 14 in which the first liquid 11, the second liquid 12, and the gas 13 are mixed, in the downstream of the liquid flow direction. Mixed liquid 1 by two-liquid mixing device 1c
Since the method of manufacturing 4 is similar to the above-described embodiment, it is substituted for this and the detailed description thereof will be omitted. In the embodiment of FIG. 4, the liquid chamber 2c and the gas chamber 3c are arranged concentrically in the horizontal direction, but may be arranged in the vertical direction. Further, the arrangement of the liquid chamber 2c and the air chamber 3c may be reversed. That is, the air chamber 3c may be arranged inside the liquid chamber 2c.

【0043】図5は本発明のさらに異なる他の実施の形
態による二液混合装置1dの概略構成を示す断面図であ
る。
FIG. 5 is a sectional view showing a schematic configuration of a two-liquid mixing apparatus 1d according to still another embodiment of the present invention.

【0044】図5に示すように、第一の液体11を通過
させる球状の液室2dが配置され、該液室2dの中心に
球状の気室3dが配置されている。液室2dに第一の液
体用供給口7dが設けられている。気室3dは多孔性の
球状隔壁6dにより囲繞され、液室2dと気室3dとは
多孔性の球状隔壁6dを介して隣接している。すなわ
ち、気室3dは多孔性の球状隔壁6dを通して液室2d
と連通している。気室3dは加圧された気体13を供給
する気体供給口8dを備え、気室3d内に第二の液体用
供給管4dとその先端に固定された第二の液体12を噴
霧する手段5、例えば噴霧ノズルを備えている。液室2
dは、第一の液体11と、第二の液体12と、気体13
とが混合された混合液14を流出する流出口10dを液
体流動方向の下流に有している。二液混合装置1dによ
り混合液14を製造する方法は上記の実施の形態におけ
る説明に類似するのでこれに代替する。また、液室2d
と気室3dとの配置を逆にしてもよい。即ち、気室3d
は液室2dの外側に配置されるようにしてもよい。
As shown in FIG. 5, a spherical liquid chamber 2d through which the first liquid 11 passes is disposed, and a spherical gas chamber 3d is disposed at the center of the liquid chamber 2d. A first liquid supply port 7d is provided in the liquid chamber 2d. The air chamber 3d is surrounded by a porous spherical partition 6d, and the liquid chamber 2d and the air chamber 3d are adjacent to each other via the porous spherical partition 6d. That is, the gas chamber 3d is connected to the liquid chamber 2d through the porous spherical partition wall 6d.
Is in communication with The gas chamber 3d is provided with a gas supply port 8d for supplying a pressurized gas 13, and means 5 for spraying the second liquid supply pipe 4d and the second liquid 12 fixed at the tip thereof into the gas chamber 3d. For example, a spray nozzle is provided. Liquid chamber 2
d is a first liquid 11, a second liquid 12, and a gas 13
Has an outlet 10d at the downstream side in the liquid flowing direction for flowing out the mixed liquid 14 in which the liquid is mixed. The method for producing the mixed liquid 14 by the two-liquid mixing apparatus 1d is similar to the description in the above-described embodiment, and will be substituted therefor. The liquid chamber 2d
And the arrangement of the air chamber 3d may be reversed. That is, the air chamber 3d
May be arranged outside the liquid chamber 2d.

【0045】[0045]

【発明の効果】本発明の二液混合装置は、前記第一の液
体を通過させる液室と、該液室に多孔性の隔壁を介して
隣接する気室と、加圧された気体を前記気室に供給する
手段と、前記気室内に前記第二の液体を供給する手段
と、を備えたので、気体を超微細に第一の液体に混合す
ることができる。
According to the present invention, there is provided a two-liquid mixing apparatus, comprising: a liquid chamber through which the first liquid passes; an air chamber adjacent to the liquid chamber via a porous partition; Since the apparatus includes the means for supplying the gas to the gas chamber and the means for supplying the second liquid to the gas chamber, the gas can be mixed with the first liquid in an ultrafine manner.

【0046】また、本発明の二液混合装置は気室内に混
合前の第二の液体を供給する手段を有することとしたの
で、気体によって第二の液体が気体とともに多孔性の隔
壁から押し出されるために、第二の液体も微細な粒子状
態で気体と同様に第一の液体に混合することが可能とな
り、二液を高速連続混合することが可能となる。
Further, since the two-liquid mixing apparatus of the present invention has means for supplying the second liquid before mixing into the gas chamber, the second liquid is pushed out of the porous partition wall together with the gas by the gas. Therefore, the second liquid can be mixed with the first liquid in the form of fine particles in the same manner as the gas, and the two liquids can be continuously mixed at a high speed.

【0047】また、本発明の二液混合装置は、液室に第
一の液体、気室に気体、さらに気室内に第二の液体を供
給する手段という構成、すなわち第二の液体を供給する
手段と第一の液体とが直接接触せず、さらに第一の液体
と第二の液体との間に気体が介在しているという構成と
したので、装置を停止させたときにノズルが第一の液体
を吸引して目詰まりを起こすということがなく、また、
第一の液体と直接接している気体排出口の多孔の閉塞を
緩和させることができる。
Further, the two-liquid mixing device of the present invention supplies the first liquid to the liquid chamber, the gas to the gas chamber, and the second liquid to the gas chamber, that is, supplies the second liquid. Since the means and the first liquid are not in direct contact with each other and a gas is interposed between the first liquid and the second liquid, when the apparatus is stopped, the nozzle is in the first position. Without causing clogging by sucking the liquid,
Blockage of the pores of the gas discharge port that is in direct contact with the first liquid can be reduced.

【0048】なお、第一の液体がある程度の大きさの固
体を含むものであっても、装置を閉鎖させることなく二
液を混合することができる。
Even if the first liquid contains a certain amount of solid, the two liquids can be mixed without closing the apparatus.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施の形態による二液混合装置の概
略図
FIG. 1 is a schematic diagram of a two-liquid mixing device according to an embodiment of the present invention.

【図2】本発明の一実施の形態による二液混合装置の概
略図
FIG. 2 is a schematic diagram of a two-liquid mixing device according to an embodiment of the present invention.

【図3】本発明の一実施の形態による二液混合装置の概
略図
FIG. 3 is a schematic diagram of a two-liquid mixing device according to an embodiment of the present invention.

【図4】本発明の一実施の形態による二液混合装置の概
略図
FIG. 4 is a schematic diagram of a two-liquid mixing device according to an embodiment of the present invention.

【図5】本発明の一実施の形態による二液混合装置の概
略図
FIG. 5 is a schematic diagram of a two-liquid mixing device according to an embodiment of the present invention.

【符号の説明】 1、1a、1b、1c、1d 二液混合装置 2 外管 2a、2b、2c、2d 液室 3 内管 3a、3b、3c、3d 気室 4、4a、4b、4c、4d 第二の液体用供給管 5 供給手段(噴霧手段) 6、6a、6b、6c、6d 多孔性の隔壁または気
体排出口 7、7a、7b、7c、7d 第一の液体用供給口 8、8a、8b、8c、8d 気体供給口 9 第二の液体用供給口 10、10a、10b、10c、10d 流出口 11 汚泥(第一の液体) 12 過酸化水素(第二の液体) 13 気体 14 混合液
[Description of Signs] 1, 1a, 1b, 1c, 1d Two-liquid mixing device 2 Outer tube 2a, 2b, 2c, 2d Liquid chamber 3 Inner tube 3a, 3b, 3c, 3d Air chamber 4, 4a, 4b, 4c, 4d second liquid supply pipe 5 supply means (spray means) 6, 6a, 6b, 6c, 6d porous partition or gas outlet 7, 7a, 7b, 7c, 7d first liquid supply 8, 8a, 8b, 8c, 8d Gas supply port 9 Second liquid supply port 10, 10a, 10b, 10c, 10d Outflow port 11 Sludge (first liquid) 12 Hydrogen peroxide (second liquid) 13 Gas 14 Mixture

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 第一の液体と第二の液体を混合する二液
混合装置において、前記第一の液体を通過させる液室
と、該液室に多孔性の隔壁を介して隣接する気室と、加
圧された気体を前記気室に供給する手段と、前記気室内
に前記第二の液体を供給する手段とを備えてなることを
特徴とする二液混合装置。
1. A two-liquid mixing apparatus for mixing a first liquid and a second liquid, wherein a liquid chamber through which the first liquid passes, and a gas chamber adjacent to the liquid chamber via a porous partition. And a means for supplying a pressurized gas to the gas chamber, and means for supplying the second liquid into the gas chamber.
【請求項2】 前記液室が曲面または平面を含む単面体
または多面体で形成され、前記気室が曲面または平面を
含む単面体または多面体の前記隔壁を介して該液室内に
少なくとも一部が配されていることを特徴とする請求項
1記載の二液混合装置。
2. The liquid chamber is formed of a monohedron or a polyhedron including a curved surface or a flat surface, and the air chamber is at least partially disposed in the liquid chamber through the monohedral or polyhedral partition including a curved surface or a flat surface. The two-liquid mixing device according to claim 1, wherein the mixing is performed.
【請求項3】 前記気室が曲面または平面を含む単面体
または多面体で形成され、前記液室が曲面または平面を
含む単面体または多面体の前記隔壁を介して該気室内に
少なくとも一部が配されていることを特徴とする請求項
1記載の二液混合装置。
3. The air chamber is formed of a monohedron or a polyhedron having a curved surface or a flat surface, and the liquid chamber is at least partially disposed in the air chamber through the monohedral or polyhedral partition having a curved surface or a flat surface. The two-liquid mixing device according to claim 1, wherein the mixing is performed.
JP11210197A 1999-04-09 1999-07-26 Two-part liquid mixing device Withdrawn JP2000350929A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP11210197A JP2000350929A (en) 1999-04-09 1999-07-26 Two-part liquid mixing device
PCT/JP2000/002221 WO2000061268A1 (en) 1999-04-09 2000-04-06 Two-liquid mixer

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP11-101927 1999-04-09
JP10192799 1999-04-09
JP11210197A JP2000350929A (en) 1999-04-09 1999-07-26 Two-part liquid mixing device

Publications (1)

Publication Number Publication Date
JP2000350929A true JP2000350929A (en) 2000-12-19

Family

ID=26442697

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (2)

Country Link
JP (1) JP2000350929A (en)
WO (1) WO2000061268A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013010065A (en) * 2011-06-28 2013-01-17 Shinei Kogyo Kk Sterilizing apparatus
CN110368824A (en) * 2018-04-13 2019-10-25 埃尔微尘科技(北京)有限公司 A kind of Liqiud-gas mixing device
WO2019233096A1 (en) * 2018-06-07 2019-12-12 埃尔微尘科技(北京)有限公司 Heat and working medium transfer device
CN110579118A (en) * 2018-06-07 2019-12-17 埃尔微尘科技(北京)有限公司 Heat exchanger

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CN110575764B (en) * 2018-06-07 2024-08-20 芙特碳汇(北京)科技有限公司 Heat and mass transfer device
CN110870982A (en) * 2018-08-31 2020-03-10 埃尔微尘科技(北京)有限公司 Evaporation device
CN115463600B (en) * 2022-10-18 2023-07-21 安徽理工大学 Efficient mixing and pulp mixing device and method for medicament and ore pulp

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4539591B1 (en) * 1967-05-01 1970-12-12
JPS5235905B2 (en) * 1974-05-29 1977-09-12
JPH06170197A (en) * 1992-12-08 1994-06-21 Kanegafuchi Chem Ind Co Ltd Fluid mixing device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013010065A (en) * 2011-06-28 2013-01-17 Shinei Kogyo Kk Sterilizing apparatus
CN110368824A (en) * 2018-04-13 2019-10-25 埃尔微尘科技(北京)有限公司 A kind of Liqiud-gas mixing device
WO2019233096A1 (en) * 2018-06-07 2019-12-12 埃尔微尘科技(北京)有限公司 Heat and working medium transfer device
CN110579118A (en) * 2018-06-07 2019-12-17 埃尔微尘科技(北京)有限公司 Heat exchanger

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