JP2006055829A - Liquid diluting/mixing/feeding apparatus - Google Patents

Liquid diluting/mixing/feeding apparatus Download PDF

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JP2006055829A
JP2006055829A JP2004272584A JP2004272584A JP2006055829A JP 2006055829 A JP2006055829 A JP 2006055829A JP 2004272584 A JP2004272584 A JP 2004272584A JP 2004272584 A JP2004272584 A JP 2004272584A JP 2006055829 A JP2006055829 A JP 2006055829A
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fluid
mixing
pipe
pressure
side hole
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Teruaki Rokuta
暉朗 六田
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Abstract

<P>PROBLEM TO BE SOLVED: To solve the problem in a method for employing a single pipe as a simple way for a mechanism used in a chemical sprayer, or the like, for diluting/mixing a fluid B with a fluid A, introduce the fluid A for dilution from one end of the pipe, and the fluid B for dilution from small holes formed in an intermediate part of the pipe, and to join and discharge the fluids from the other end, thereby makes it hard to uniform the small holes for introducing the fluid B to be diluted because their diameters are very small. <P>SOLUTION: The subject liquid diluting/mixing/feeding apparatus employs a single pipe. The fluid B to be diluted is introduced into one end of the pipe. The pipe is provided with an inner diameter and a length sufficient to enable an easy setting of a uniform flow rate. A side hole having a large diameter comparatively easy to prepare is formed in a part of the pipe nearer to the other end side. The fluid A for dilution is introduced through the side hole and joined. The joined fluid is discharged from the other end. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は、噴霧器の主部品の一つとして用いる噴霧器容器に関する。  The present invention relates to a sprayer container used as one of main components of a sprayer.

従来の噴霧液の希釈法の一つは、図３に示すように、希釈する液である水道水（１３）が流入口（１６）に流入し、その流れの途中の小側孔（２０）から稀釈される液である薬液（１８）が微量ずつ流入合流する機構であった。従って小側孔（２０）は微小であり、その口径を多数の製品に均一に作成することは容易でなかった。
また、混和管（１７）は袋（１４）を貫通する形になっている。
特開〔２００４−１２９６３０〕の〔請求項３〕 また図４で、一種のエアゾル方式の噴霧器とも見なせる希釈する流体として気体を使用する方法では、液相部（２７ｂ）の希釈される液が小側孔（２６ｂ）から混合細管（２６）に流入する機構になっており、小側孔（２６ｂ）は微小であることを要し、多数製品に均一に作成することは容易でなかった。 また、希釈する流体としての気体が流れる混合細管（２６）の途中の小側孔（２６ｂ）に、液相部（２７ｂ）の液が流入合流する機構のため、管はＶ字状となっている。 特開〔２００２−３４６４４０〕の〔請求項１〕 As shown in FIG. 3, in the conventional method for diluting the spray liquid, tap water (13), which is a liquid to be diluted, flows into the inlet (16), and a small side hole (20) in the middle of the flow. It was a mechanism in which the chemical solution (18), which is a diluted solution, flows in and joins in small amounts. Therefore, the small side hole (20) is very small, and it has not been easy to make its diameter uniformly in many products.
Further, the mixing tube (17) is formed so as to penetrate the bag (14).
[Claim 3] of JP-A-2004-129630 Further, in FIG. 4, in the method of using a gas as a diluting fluid that can be regarded as a kind of aerosol type sprayer, the liquid to be diluted in the liquid phase part (27b) is small. It is a mechanism that flows from the side hole (26b) into the mixed thin tube (26), and the small side hole (26b) needs to be minute, and it was not easy to make it uniformly in many products. In addition, the pipe is V-shaped because of the mechanism in which the liquid in the liquid phase part (27b) flows into the small side hole (26b) in the middle of the mixed thin pipe (26) through which the gas as the fluid to be diluted flows. Yes. [Claim 1] of JP-A-2002-346440

そこでこの発明は、図３の小側孔（２０）あるいは図４の小側孔（２６ｂ）として微小側孔を製品化に際して均一に作成することは容易でなく、不均一になると意図する希釈倍率を作れず、また、単位時間内の薬液噴霧量も製品間で一定しないという問題の解決を課題とする。また、構造的により簡単な方法が望ましい。  Therefore, according to the present invention, it is not easy to make a minute side hole as a small side hole (20) in FIG. 3 or a small side hole (26b) in FIG. The problem is to solve the problem that the amount of chemical spray within a unit time is not constant between products. Also, a structurally simpler method is desirable.

以上の課題を解決するために第一発明は、容器（１）内に、希釈する流体Ａ（４ａ）と袋（４ｃ）内に希釈される流体Ｂ（４ｂ）があり、袋（４ｃ）は内外流体の混和を防ぐが圧伝達十分な柔軟性を有する。混和管（３）の噴出口（３ｃ）は容器（１）外に、側孔（３ｂ）部は流体Ａ（４ａ）内に、流入口（３ａ）は流体Ｂ（４ｂ）内に位置させる。流体Ａ（４ａ）の圧力流入管（２）は、容器（１）外から流体Ａ（４ａ）に開口し、使用時に流体Ａ（４ａ）が圧入される。流体Ｂ（４ｂ）は、流入口（３ａ）から持続的に微量流入するが、そのためには流路に大きな抵抗を要し、流入口（３ａ）から側孔（３ｂ）部近くに至る流路抵抗部（３ｄ）は、その管の内径と長さを決めることで設定し易くする。
流体Ａ（４ａ）が圧力流入管（２）から容器（１）内に圧入されると、流体Ａ（４ａ）は混和管（３）の側孔（３ｂ）に流入し、同時に流体Ｂ（４ｂ）も流入口（３ａ）に流入し、混和管（３）の噴出口（３ｃ）から、流体Ｂ（４ｂ）が流体Ａ（４ａ）により希釈されて噴出する機構を特徴とする流体希釈混和供給装置。
また第二発明は、請求項１記載の流体Ａ（４ａ）を水道水とし、流体Ｂ（４ｂ）を農薬とし、圧力流入管（２）に水道を直接接続し、水道圧利用の噴霧器用薬液希釈兼供給装置として用いるところの請求項１記載の流体希釈混和供給装置。
第三発明は、請求項１記載の流体Ａ（４ａ）を気体とし、流体Ｂ（４ｂ）を液体とし、混和防止の袋（４ｃ）を省き、流体Ａの圧力流入管（２）に圧縮気体を接続し、噴霧器用気液混合装置として用いるところの請求項１記載の流体希釈混和供給装置。
また、第四発明は、請求項１記載の流体Ａ（４ａ）を酸素とし、流体Ｂ（４ｂ）を薬液とし、混和防止の袋（４ｃ）を省き、圧力流入管（２）に圧縮酸素を接続し、医療用の噴霧器用気液混合装置として用いるところの請求項１記載の流体希釈混和供給装置。In order to solve the above problems, the first invention includes a fluid A (4a) to be diluted and a fluid B (4b) to be diluted in a bag (4c) in the container (1). Prevents mixing of internal and external fluids, but has sufficient flexibility to transmit pressure. The spout (3c) of the mixing tube (3) is located outside the container (1), the side hole (3b) is located in the fluid A (4a), and the inlet (3a) is located in the fluid B (4b). The pressure inflow pipe (2) of the fluid A (4a) opens from the outside of the container (1) to the fluid A (4a), and the fluid A (4a) is press-fitted during use. The fluid B (4b) continuously flows in a small amount from the inflow port (3a). For this purpose, a large resistance is required for the flow path, and the flow path extends from the inflow port (3a) to the side hole (3b). The resistance portion (3d) is easily set by determining the inner diameter and length of the tube.
When the fluid A (4a) is press-fitted into the container (1) from the pressure inflow pipe (2), the fluid A (4a) flows into the side hole (3b) of the mixing tube (3) and at the same time the fluid B (4b ) Also flows into the inflow port (3a), and the fluid dilution mixing supply is characterized in that the fluid B (4b) is diluted with the fluid A (4a) and ejected from the ejection port (3c) of the mixing tube (3) apparatus.
The second invention is a chemical solution for a nebulizer using water pressure, wherein the fluid A (4a) according to claim 1 is tap water, the fluid B (4b) is pesticide, and water is directly connected to the pressure inlet pipe (2). The fluid dilution mixing and feeding apparatus according to claim 1, which is used as a dilution and feeding apparatus.
According to a third aspect of the present invention, the fluid A (4a) according to claim 1 is gas, the fluid B (4b) is liquid, the miscibility prevention bag (4c) is omitted, and the compressed gas is supplied to the pressure inflow pipe (2) of the fluid A. The fluid dilution mixing and feeding device according to claim 1, wherein the fluid dilution mixing and feeding device is used as a gas-liquid mixing device for a sprayer.
According to a fourth aspect of the present invention, the fluid A (4a) according to claim 1 is oxygen, the fluid B (4b) is a chemical solution, the anti-mixing bag (4c) is omitted, and compressed oxygen is supplied to the pressure inlet pipe (2). The fluid dilution mixing supply device according to claim 1, which is connected and used as a gas-liquid mixing device for a medical nebulizer.

第一発明、または第二発明によれば、目的とする希釈倍率を得やすく、且つ数を製作した場合により均一な製品が得られる。又構造的にも簡単で製作しやすい。  According to the first invention or the second invention, it is easy to obtain a target dilution factor, and a more uniform product can be obtained when the number is manufactured. In addition, it is simple in structure and easy to manufacture.

第三発明、第四発明によれば、気体と液体の一種の混和を、液体を気体で希釈すると見なせば、その希釈倍率の調節が従来より容易で、噴霧器の霧の質を調節しやすく、又数を製作した場合にもより均一な品が得られる。構造的にも単純化され、製作しやすい。  According to the third and fourth inventions, if one kind of mixing of gas and liquid is regarded as diluting the liquid with gas, it is easier to adjust the dilution ratio than before, and it is easy to adjust the quality of the mist of the sprayer. In addition, a more uniform product can be obtained when the number is manufactured. It is simplified in structure and easy to manufacture.

以下に、実施例に基づいて本発明をより詳細に説明するが、本発明はこれらの実施例によって限定されるものではない。  Hereinafter, the present invention will be described in more detail based on examples, but the present invention is not limited to these examples.

実施例１、この発明の一実施形態を、図１に示す。
耐圧性の容器（１）内に、希釈する流体Ａ（４ａ）として水道水と、袋（４ｃ）内に希釈される流体Ｂ（４ｂ）として農薬があり、袋（４ｃ）は内外流体の混和を防ぐが圧伝達十分な柔軟性を有する。混和管（３）の一端の噴出口（３ｃ）は容器（１）外に、側孔（３ｂ）は流体Ａ（４ａ）の水道水内に、流入口（３ａ）は袋（４ｃ）内の流体Ｂ（４ｂ）の農薬中に位置させる。流体Ａ（４ａ）の水道水の圧力流入管（２）は、容器（１）外から流体Ａ（４ａ）の水道水中に開口し、使用時には水道が接続され圧入される。流体Ｂ（４ｂ）の農薬は、混和管（３）の流入口（３ａ）から流入するが、微量にするために、流入口（３ａ）から側孔（３ｂ）部近くに至る流路抵抗部（３ｄ）の抵抗を大きくする必要があるが、その部分の管の内径と長さで決められ、設定はより容易になされる。
流体Ａ（４ａ）の水道水が圧力流入管（２）から容器（１）内に圧入されると、流体Ａ（４ａ）の水道水は混和管（３）の側孔（３ｂ）に流入し、同時に流体Ｂ（４ｂ）の農薬も流入口（３ａ）に流入し、混和管（３）の容器（１）外にある噴出口（３ｃ）から、流体Ｂ（４ｂ）の農薬が流体Ａ（４ａ）の水道水により希釈されて噴出する機構を特徴とする流体希釈混和供給装置。
従来の噴霧液の希釈法の一つは、図３に示すように水道水（１３）が混和管（１７）の流入口（１６）に流入後、小側孔（２０）から薬液（１８）を流入合流させる様式であった。従って水道水の、混和管（１７）中の流量に対して、薬液（１８）の小側孔（２０）への流入量は微量なことが必要で、微小な小側孔（２０）の作成が必要である。その作成が必ずしも容易でなく、特に多数の製品を作る際に均一性が問題であった。
また、図３において、従来の流入口（１６）に始まる混和管（１７）は、袋（１４）を貫通する形になり、やや複雑となっている。Example 1 An embodiment of the present invention is shown in FIG.
In the pressure-resistant container (1), there is tap water as the fluid A (4a) to be diluted and pesticides as the fluid B (4b) to be diluted in the bag (4c), and the bag (4c) is a mixture of internal and external fluids. The pressure transmission has sufficient flexibility. The outlet (3c) at one end of the mixing tube (3) is outside the container (1), the side hole (3b) is in the tap water of the fluid A (4a), and the inlet (3a) is in the bag (4c). Located in pesticide in fluid B (4b). The tap water pressure inflow pipe (2) of the fluid A (4a) opens from the outside of the container (1) into the tap water of the fluid A (4a), and the tap water is connected and press-fitted in use. The pesticide of the fluid B (4b) flows in from the inlet (3a) of the mixing tube (3), but in order to make it a very small amount, the flow path resistance portion extending from the inlet (3a) to the vicinity of the side hole (3b) portion Although it is necessary to increase the resistance of (3d), it is determined by the inner diameter and length of the tube in that portion, and the setting is made easier.
When tap water of fluid A (4a) is pressed into the container (1) from the pressure inlet pipe (2), tap water of fluid A (4a) flows into the side hole (3b) of the mixing pipe (3). At the same time, the pesticide in the fluid B (4b) also flows into the inlet (3a), and the pesticide in the fluid B (4b) flows from the spout (3c) outside the container (1) of the mixing tube (3) to the fluid A ( 4a) A fluid dilution mixing and feeding apparatus characterized in that it is diluted with tap water and ejected.
As shown in FIG. 3, one of the conventional methods for diluting the spray liquid is that the tap water (13) flows into the inlet (16) of the mixing tube (17) and then the chemical liquid (18) from the small side hole (20). It was the style which made the inflow merge. Therefore, it is necessary for the flow rate of the tap water to flow into the small side hole (20) of the chemical solution (18) with respect to the flow rate in the mixing tube (17). is required. Its creation is not always easy, and uniformity has been a problem, especially when many products are made.
Moreover, in FIG. 3, the mixing tube (17) starting from the conventional inlet (16) is shaped to penetrate the bag (14) and is somewhat complicated.

図１の噴出口（３ｃ）に、図５に示す噴霧ノズル（３１）を先端に付けた管の混和流体流入口（２８）を接続することによって、噴霧器部品として流体希釈混和供給装置の機能を発揮する。  1 is connected to the mixing fluid inlet (28) of the tube having the spray nozzle (31) shown in FIG. 5 attached to the tip thereof, so that the function of the fluid dilution mixing supply device as a sprayer component can be achieved. Demonstrate.

図１の袋（４ｃ）は、容器（１）の内圧を流体Ａ（４ａ）の水道水と同様に受け、混和を防止できる隔壁に代えることができる。  The bag (4c) in FIG. 1 receives the internal pressure of the container (1) in the same manner as the tap water of the fluid A (4a), and can be replaced with a partition wall that can prevent mixing.

容器（１）は、耐圧性で、流体Ｂ（４ｂ）の農薬の残量を知りうるために、内部を透視可能な材質とする。  The container (1) is pressure resistant and is made of a material that allows the inside to be seen through in order to know the remaining amount of pesticide in the fluid B (4b).

「実施形態の効果」
この実施形態によれば、図１の希釈される流体Ｂ（４ｂ）の農薬の混和管（３）への流入量が、従来の図３の小側孔（２０）のように口径で決まるのでなく、流路抵抗部（３ｄ）の抵抗、即ちその管の内径と、長さで調整可能となり、製作がより容易、且つ製品の均一性が得られやすい。
また、図１の混和管（３）の流入口（３ａ）が、袋（４ｃ）に挿入された形になり、従来の図３の混和管（３）が袋（４ｃ）を貫通するよりも製作が容易になる。"Effect of embodiment"
According to this embodiment, the amount of fluid B (4b) diluted in FIG. 1 into the agrochemical mixing tube (3) is determined by the diameter as in the conventional small side hole (20) in FIG. However, it is possible to adjust the resistance of the flow path resistance portion (3d), that is, the inner diameter and the length of the tube, and it is easier to manufacture and to obtain product uniformity.
Further, the inlet (3a) of the mixing tube (3) in FIG. 1 is inserted into the bag (4c), so that the conventional mixing tube (3) in FIG. 3 penetrates the bag (4c). Easy to manufacture.

実施例２、この発明の一実施形態を、図２に示す。
耐圧性の容器（６）内に、気体（９ａ）と液体（９ｂ）が容れられ、混和細管（８）の噴出口（８ｃ）は容器（６）外に、側孔（８ｂ）は気体（９ａ）内に、流入口（８ａ）は液体（９ｂ）の最深部に位置させる。圧力気体流入管（７）は、気体（９ａ）に開口しており、そこに圧縮気体が流入すと、気体（９ａ）は側孔（８ｂ）に流入し、同時に液体（９ｂ）も流入口（８ａ）に流入し、噴出口（８ｃ）から、気体（９ａ）により液体（９ｂ）がエアゾル化し霧となり噴出する。液体（９ｂ）が、流入口（８ａ）から微量ずつ流入するために、流入口（８ａ）から側孔（８ｂ）部近くに至る流路抵抗部（８ｄ）の抵抗を大きくする必要があるが、その部分の管の内径と長さで決められ、設定を容易とする。Example 2 FIG. 2 shows an embodiment of the present invention.
Gas (9a) and liquid (9b) are contained in the pressure-resistant container (6), the spout (8c) of the mixing tube (8) is outside the container (6), and the side hole (8b) is gas ( 9a), the inlet (8a) is located at the deepest part of the liquid (9b). The pressure gas inflow pipe (7) opens to the gas (9a), and when compressed gas flows into the gas (9a), the gas (9a) flows into the side hole (8b) and at the same time the liquid (9b) also flows into the inlet. It flows into (8a), and the liquid (9b) is aerosolized by the gas (9a) from the jet outlet (8c), and is sprayed as mist. Since the liquid (9b) flows in a small amount from the inlet (8a), it is necessary to increase the resistance of the flow path resistance portion (8d) extending from the inlet (8a) to the vicinity of the side hole (8b). , Which is determined by the inner diameter and length of the tube at that portion, making it easy to set.

噴出口（８ｃ）を狭小に、ピンホール化することにより、霧粒子はより細かくなる。  By making the spout (8c) narrow and pinhole, the mist particles become finer.

噴出口（８ｃ）に、長い可撓性細管を接続し、その抵抗増に見合ったより高圧の気体を圧力気体流入管（７）に送れば、長い可撓性細管の先端からでも噴霧可能である。  If a long flexible thin tube is connected to the spout (8c) and a higher pressure gas corresponding to the increase in resistance is sent to the pressure gas inflow tube (7), spraying is possible even from the tip of the long flexible thin tube. .

「実施形態の効果」
この実施形態によれば、図２の液体（９ｂ）の流入口（８ａ）への流入速度は、従来の図４の小側孔（２６ｂ）の様に口径で決まるのでなく、図２の流路抵抗部（８ｄ）の抵抗、即ち管の内径と、長さで調整でき、製作が容易となり、製品の均一性に役立つ。
また、従来の図４、容器（２４）内のＶ字状の混合細管（２６）は、図２の混合細管（８）の如く、一本の管となり、この点でも簡略化される。"Effect of embodiment"
According to this embodiment, the inflow speed of the liquid (9b) in FIG. 2 to the inlet (8a) is not determined by the diameter as in the conventional small side hole (26b) in FIG. It can be adjusted by the resistance of the path resistance portion (8d), that is, the inner diameter and the length of the tube, facilitating the production and helping the product uniformity.
Also, the conventional V-shaped mixing tube (26) in the container (24) in FIG. 4 becomes a single tube like the mixing tube (8) in FIG. 2, and this is also simplified.

この発明の実施例１の形態を示す断面図である。It is sectional drawing which shows the form of Example 1 of this invention. この発明の実施例２の形態を示す断面図である。It is sectional drawing which shows the form of Example 2 of this invention. 従来技術、Conventional technology, 特開〔２００４−１２９６３０〕の〔請求項３〕を示す断面図である。It is sectional drawing which shows [Claim 3] of Unexamined-Japanese-Patent No. 2004-129630.

図４FIG.

従来技術、 特開〔２００２−３４６４４０〕の〔請求項１〕を示す断面図である。 Conventional technology, It is sectional drawing which shows [Claim 1] of Unexamined-Japanese-Patent No. 2002-346440.

図５FIG.

この発明の実施例１に接続する付属部品の従来技術、 特開〔２００４−１２９６３０〕の〔請求項３〕の断面図である。 Prior art of accessory parts connected to Example 1 of the present invention, It is sectional drawing of [Claim 3] of Unexamined-Japanese-Patent No. 2004-129630.

符号の説明Explanation of symbols

１ 容器 ２ 圧力流入管
３ 混和管 ３ａ 流入口
３ｂ 側孔 ３ｃ 噴出口
３ｄ 流路抵抗部 ４ａ 流体Ａ
４ｂ 流体Ｂ ４ｃ 袋
５ 容器蓋DESCRIPTION OF SYMBOLS 1 Container 2 Pressure inlet pipe 3 Mixing pipe 3a Inlet 3b Side hole 3c Outlet 3d Flow path resistance part 4a Fluid A
4b Fluid B 4c Bag 5 Container lid

６ 容器 ７ 圧力気体流入管
８ 混和細管 ８ａ 流入口
８ｂ 側孔 ８ｃ 噴出口
８ｄ 流路抵抗部 ９ａ 気体
９ｂ 液体6 Container 7 Pressure gas inflow pipe 8 Mixing thin tube 8a Inlet 8b Side hole 8c Spout 8d Flow path resistance 9a Gas 9b Liquid

１０ 薬液注入口 １１ 容器蓋
１２ 容器 １３ 水道水
１４ 袋 １５ 水道流入管
１６ 流入口 １７ 混和管
１８ 薬液 １９ 硬性網状カバー
２０ 小側孔 ２１ 混和部
２２ 開閉コック ２３ 噴霧ノズルDESCRIPTION OF SYMBOLS 10 Chemical liquid inlet 11 Container lid 12 Container 13 Tap water 14 Bag 15 Water inlet pipe 16 Inlet 17 Mixing pipe 18 Chemical liquid 19 Hard net-like cover 20 Small side hole 21 Mixing part 22 Opening cock 23 Spray nozzle

２４ 容器 ２５ 圧力気体流入管
２６ 混合細管 ２６ａ 流入口
２６ｂ 小側孔 ２６ｃ 噴出口
２７ａ 気相部 ２７ｂ 液相部24 Vessel 25 Pressure gas inflow pipe 26 Mixing narrow pipe 26a Inlet 26b Small side hole 26c Outlet 27a Gas phase part 27b Liquid phase part

２８ 混和流体流入口 ２９ 混和部
３０ 開閉コック ３１ 噴霧ノズル28 Mixing fluid inlet 29 Mixing section 30 Opening / closing cock 31 Spray nozzle

Claims (4)

容器（１）内に、希釈する流体Ａ（４ａ）と袋（４ｃ）内に希釈される流体Ｂ（４ｂ）があり、袋（４ｃ）は内外流体の混和を防ぐが圧伝達十分な柔軟性を有する。
混和管（３）の噴出口（３ｃ）は容器（１）外に、側孔（３ｂ）部は流体Ａ（４ａ）内に、流入口（３ａ）は流体Ｂ（４ｂ）内に位置させる。圧力流入管（２）は、容器（１）外から流体Ａ（４ａ）に開口し、作動時に流体Ａ（４ａ）が圧入される。流体Ｂ（４ｂ）は、流入口（３ａ）から持続的に微量流入するが、そのためには流路に大きな抵抗を要し、流入口（３ａ）から側孔（３ｂ）部近くに至る流路抵抗部（３ｄ）は、その管の内径と長さを決めることで設定をより容易とする。
流体Ａ（４ａ）が圧力流入管（２）から容器（１）内に圧入されると、流体Ａ（４ａ）は混和管（３）の側孔（３ｂ）に流入し、同時に流体Ｂ（４ｂ）も流入口（３ａ）に流入し、混和管（３）の噴出口（３ｃ）から、流体Ｂ（４ｂ）が流体Ａ（４ａ）により希釈されて噴出する機構を特徴とする流体希釈混和供給装置。In the container (1), there are a fluid A (4a) to be diluted and a fluid B (4b) to be diluted in a bag (4c). The bag (4c) prevents mixing of the inner and outer fluids but is flexible enough to transmit pressure. Have
The spout (3c) of the mixing tube (3) is located outside the container (1), the side hole (3b) is located in the fluid A (4a), and the inlet (3a) is located in the fluid B (4b). The pressure inflow pipe (2) opens from the outside of the container (1) to the fluid A (4a), and the fluid A (4a) is press-fitted during operation. The fluid B (4b) continuously flows in a small amount from the inflow port (3a). For this purpose, a large resistance is required for the flow path, and the flow path extends from the inflow port (3a) to the side hole (3b). The resistance portion (3d) can be easily set by determining the inner diameter and length of the tube.
When the fluid A (4a) is press-fitted into the container (1) from the pressure inflow pipe (2), the fluid A (4a) flows into the side hole (3b) of the mixing tube (3) and at the same time the fluid B (4b ) Also flows into the inflow port (3a), and the fluid dilution mixing supply is characterized in that the fluid B (4b) is diluted with the fluid A (4a) and ejected from the ejection port (3c) of the mixing tube (3) apparatus. 請求項１記載の流体Ａ（４ａ）を水道水とし、流体Ｂ（４ｂ）を農薬とし、圧力流入管（２）に水道を直接接続し、水道圧利用の噴霧器用薬液希釈兼供給装置として用いるところの請求項１記載の流体希釈混和供給装置。  The fluid A (4a) according to claim 1 is tap water, the fluid B (4b) is a pesticide, and the water is directly connected to the pressure inflow pipe (2) to be used as a chemical solution dilution and supply device for a sprayer using water pressure. However, the fluid dilution mixing supply apparatus according to claim 1. 請求項１記載の流体Ａ（４ａ）を気体とし、流体Ｂ（４ｂ）を液体とし、混和防止の袋（４ｃ）を省き、圧力流入管（２）に圧縮気体を接続し、一種のエアゾル型噴霧器の気液混合装置として用いるところの請求項１記載の流体希釈混和供給装置。  The fluid A (4a) according to claim 1 is a gas, the fluid B (4b) is a liquid, the miscibility prevention bag (4c) is omitted, a compressed gas is connected to the pressure inlet pipe (2), and a kind of aerosol type The fluid dilution mixing supply device according to claim 1, which is used as a gas-liquid mixing device of a sprayer. 請求項１記載の流体Ａ（４ａ）を酸素とし、流体Ｂ（４ｂ）を薬液とし、混和防止の袋（４ｃ）を省き、圧力流入管（２）に圧縮酸素を接続し、医療用の噴霧器用気液混合装置として用いるところの請求項１記載の流体希釈混和供給装置。  The fluid A (4a) according to claim 1 is oxygen, the fluid B (4b) is chemical, the miscibility prevention bag (4c) is omitted, and compressed oxygen is connected to the pressure inflow pipe (2). The fluid dilution mixing and feeding apparatus according to claim 1, which is used as a gas-liquid mixing apparatus.
JP2004272584A 2004-08-23 2004-08-23 Liquid diluting/mixing/feeding apparatus Pending JP2006055829A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004272584A JP2006055829A (en) 2004-08-23 2004-08-23 Liquid diluting/mixing/feeding apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004272584A JP2006055829A (en) 2004-08-23 2004-08-23 Liquid diluting/mixing/feeding apparatus

Publications (1)

Publication Number Publication Date
JP2006055829A true JP2006055829A (en) 2006-03-02

Family

ID=36103750

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004272584A Pending JP2006055829A (en) 2004-08-23 2004-08-23 Liquid diluting/mixing/feeding apparatus

Country Status (1)

Country Link
JP (1) JP2006055829A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117110560A (en) * 2023-08-01 2023-11-24 广东万田检测股份有限公司 Device and method for rapidly detecting content of quinolone drugs in bee products

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117110560A (en) * 2023-08-01 2023-11-24 广东万田检测股份有限公司 Device and method for rapidly detecting content of quinolone drugs in bee products
CN117110560B (en) * 2023-08-01 2024-03-19 广东万田检测股份有限公司 Device and method for rapidly detecting content of quinolone drugs in bee products

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