JPH0760170A - Liquid atomizer - Google Patents

Liquid atomizer

Info

Publication number
JPH0760170A
JPH0760170A JP20930093A JP20930093A JPH0760170A JP H0760170 A JPH0760170 A JP H0760170A JP 20930093 A JP20930093 A JP 20930093A JP 20930093 A JP20930093 A JP 20930093A JP H0760170 A JPH0760170 A JP H0760170A
Authority
JP
Japan
Prior art keywords
liquid
swirl
liquid supply
circular
chamber
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.)
Pending
Application number
JP20930093A
Other languages
Japanese (ja)
Inventor
Katsuhiko Uno
克彦 宇野
Tomomichi Asou
智倫 麻生
Katsuhiko Ishikawa
克彦 石川
Norio Yotsuya
規夫 肆矢
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP20930093A priority Critical patent/JPH0760170A/en
Publication of JPH0760170A publication Critical patent/JPH0760170A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain spray of uniform particle diameter in the wide range of control of the atomized quantity by installing a circular chamber, a jet hole, circular introducing passes, liquid feeding pipes for feeding liquid from separate routes, valve discs of the liquid feeding pipes, and a liquid feeding part for feeding liquid to the liquid feeding pipes in its compressed state. CONSTITUTION:A liquid is sucked from a tank 6 and fed to liquid feeding pipes 8a, 8b in its compressed state. The liquid from the liquid feeding pipe 8a arrives in a liquid chamber 10 of a body 9 and is fed to a circular chamber 16 from a circular introducing pass 15a, and the liquid fed from the liquid feeding pipe 8b is fed to the circular chamber 16 from the circular introducing pass 15b. The circular introducing passes 15a, 15b are tangentially installed to the circular chamber 16. Therefore, the liquid in the circular chamber 16 is given turning force and its turning force is increased as it advances toward the center. It is jetted as a turning liquid film 18 from a jet hole 17 installed downstream of the circular chamber 16, and atomized by the shear forcing due to the relative velocity difference between the jet velocity and the turning velocity of the liquid film 18 to surrounding air.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、例えば加湿器、医療機
器、燃焼機器等に利用され、水、油、薬溶液などを微粒
化する液体微粒化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 liquid atomizer which is used, for example, in humidifiers, medical equipment, combustion equipment and the like to atomize water, oil, chemical solutions and the like.

【0002】[0002]

【従来の技術】液体の微粒化は色々な分野で用いられて
おり、微粒化手段も多岐にわたっている。この微粒化手
段としては、液体を加圧し、旋回液膜を形成して噴霧す
る圧力噴霧方式がよく使われている。圧力噴霧方式の液
体微粒化装置は、図5に示すように、加圧ポンプ1によ
り加圧状態で供給された液体が、旋回溝2から旋回室3
に到り、この旋回室3で旋回力を与えられ、旋回状態で
噴孔4から噴出される。液体の噴出速度および旋回速度
と周囲空気との相対速度差によって中空の逆円錐膜5に
生じるせん断力によって液膜5を分断し微粒化するもの
である。
2. Description of the Related Art Atomization of liquids is used in various fields, and there are various kinds of atomization means. As the atomizing means, a pressure spray method in which a liquid is pressurized to form a swirling liquid film and sprayed is often used. In the pressure atomization type liquid atomizer, as shown in FIG. 5, the liquid supplied in a pressurized state by the pressurizing pump 1 flows from the swirling groove 2 to the swirling chamber 3.
Then, a swirl force is applied in the swirl chamber 3, and the swirl chamber 3 ejects the swirl force from the injection hole 4. The liquid film 5 is divided and atomized by the shearing force generated in the hollow inverted conical film 5 due to the relative velocity difference between the jetting speed and swirling speed of the liquid and the ambient air.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来の圧
力噴霧方式の微粒化装置は、加圧ポンプ1の圧力を下げ
て霧化量を小さくすると液体流量が少なくなり、噴孔4
から噴出される液体の噴出速度および旋回速度が減少す
るので、中空の逆円錐の液膜5の液膜厚さが厚くなると
ともに、周囲との相対速度差が小さくなり、液膜に作用
するせん断力も低下する結果、粒子径が粗大化して霧化
状態が悪化する。したがって圧力ポンプ1の圧力の可変
領域内である程度の調節はできるものの、霧化量の調節
幅を大きくとれないという課題があった。
However, in the above-mentioned conventional atomization apparatus of the pressure atomization system, when the pressure of the pressurizing pump 1 is reduced to reduce the atomization amount, the liquid flow rate decreases, and the injection hole 4 is formed.
Since the jetting speed and the swirling speed of the liquid jetted from the liquid are reduced, the liquid film thickness of the hollow inverted-cone liquid film 5 becomes thicker, and the relative velocity difference with the surroundings becomes smaller, and the shear acting on the liquid film becomes smaller. As a result of the reduced force, the particle size becomes coarse and the atomized state deteriorates. Therefore, although the pressure of the pressure pump 1 can be adjusted to some extent within the variable region, there is a problem that the adjustment range of the atomization amount cannot be made large.

【0004】本発明は上記課題を解決するもので、微粒
化特性を改良し、霧化量の広い調節範囲で均一な粒子径
の噴霧を得ることのできる液体微粒化装置を提供するも
のである。
The present invention solves the above problems, and provides a liquid atomizing apparatus capable of improving atomization characteristics and obtaining a spray having a uniform particle size in a wide control range of atomization amount. .

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、請求項1では液体が充填される旋回室、この旋回室
下流側に設けられた噴出孔と、前記旋回室に旋回流れを
発生させるように液体を導入する複数の旋回導入路と、
この旋回導入路に各々別経路から液体を供給する液体供
給管と、前記各々の液体供給管の経路に設けられた弁体
と、前記液体供給管に加圧状態で液体を供給する液体供
給部を有する構成としている。
In order to achieve the above object, according to a first aspect of the present invention, a swirl chamber filled with liquid, an ejection hole provided on the downstream side of the swirl chamber, and a swirl flow are generated in the swirl chamber. A plurality of swirl introduction paths for introducing the liquid,
Liquid supply pipes for supplying liquid to the swirl introduction passages from different paths, valve bodies provided in the passages of the respective liquid supply pipes, and liquid supply unit for supplying liquid to the liquid supply pipes under pressure. It is configured to have.

【0006】また、請求項2では液体が充填される旋回
室と、この旋回室下流側に設けられた噴出孔と、前記旋
回室に旋回流れを発生させるように液体を導入する複数
の旋回導入路と、この旋回導入路に各々別経路から液体
を供給する液体供給管と、前記各々の液体供給管に設け
られ、加圧状態で液体を供給する複数個の液体供給部を
有する構成としている。
Further, according to a second aspect of the present invention, the swirl chamber filled with the liquid, the ejection holes provided on the downstream side of the swirl chamber, and the plurality of swirl introductions for introducing the liquid so as to generate the swirl flow in the swirl chamber. A passage, a liquid supply pipe for supplying liquid to each of the swirl introduction passages from a different route, and a plurality of liquid supply units provided in each of the liquid supply pipes for supplying the liquid in a pressurized state. .

【0007】[0007]

【作用】本発明は請求項1の構成によって、各供給管の
弁体を開閉することにより、同一の加圧状態で、それぞ
れの旋回室導入路から旋回室に供給される液体の量を調
節することにより、液体供給量を変化させても旋回室で
の旋回状態を一定に保つことができるので、噴霧量の広
い調節範囲で良好な噴霧状態を得ることができる。
According to the present invention, the amount of the liquid supplied from the respective swirl chamber introduction passages to the swirl chamber is adjusted under the same pressurization condition by opening and closing the valve element of each supply pipe. By doing so, the swirl state in the swirl chamber can be kept constant even if the liquid supply amount is changed, so that a good spray state can be obtained in a wide adjustment range of the spray amount.

【0008】また、請求項2の構成によれば各液体供給
管に供給される液体を、それぞれの液供給部で調節する
ことができるので噴霧量の調節をより細やかに行なうこ
とができる。
Further, according to the second aspect of the invention, since the liquid supplied to each liquid supply pipe can be adjusted by each liquid supply section, the spray amount can be adjusted more finely.

【0009】[0009]

【実施例】以下本発明の実施例を添付図面に基づいて説
明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

【0010】図1は請求項1の液体微粒化装置の一実施
例を示したものである。液体はタンク6から液体供給部
7で吸い上げられ液体供給管8a、8bに加圧状態で供
給される。液体供給管8aから供給された液体はボディ
9内の液室10に至り、旋回室押え11に設けられた液
通路12を通してボディ9先端方向へ供給される。液体
供給管8bには弁体13が設けられている。液体供給管
8aから供給された液体は、ボディ9先端のノズルヘッ
ド14に設けられた旋回導入路15aから旋回室16に
供給される。同様に液体供給管8bから供給された液体
は、ノズルヘッド14に設けられた旋回導入路15bか
ら旋回室16に供給される。旋回室16はその底面を旋
回室押え11で遮蔽することによって形成されている。
旋回導入路15a、15bは旋回室16に対して接線方
向に設けられており、したがって、旋回室16に供給さ
れた液体は旋回力を与えられ、中心に進むにしたがっ
て、旋回力を増大させながら旋回室16下流に設けられ
た噴出孔17から旋回液膜18として噴出され、液膜1
8の噴出速度および旋回速度と周囲空気の相対速度差に
よるせん断力によって微粒化される。
FIG. 1 shows an embodiment of the liquid atomizer of claim 1. The liquid is sucked up from the tank 6 by the liquid supply unit 7 and is supplied to the liquid supply pipes 8a and 8b under pressure. The liquid supplied from the liquid supply pipe 8a reaches the liquid chamber 10 in the body 9, and is supplied in the tip direction of the body 9 through the liquid passage 12 provided in the swirl chamber retainer 11. A valve body 13 is provided on the liquid supply pipe 8b. The liquid supplied from the liquid supply pipe 8 a is supplied to the swirl chamber 16 from the swirl introduction passage 15 a provided in the nozzle head 14 at the tip of the body 9. Similarly, the liquid supplied from the liquid supply pipe 8b is supplied to the swirl chamber 16 from the swirl introduction passage 15b provided in the nozzle head 14. The swirl chamber 16 is formed by shielding the bottom surface thereof with the swirl chamber retainer 11.
The swirl introduction passages 15a and 15b are provided in a tangential direction to the swirl chamber 16, and therefore, the liquid supplied to the swirl chamber 16 is given a swirl force, and the swirl force is increased as the liquid proceeds to the center. The swirl liquid film 18 is jetted from a jet hole 17 provided downstream of the swirl chamber 16 to form the liquid film 1
It is atomized by the shearing force due to the difference in relative velocity between the jetting speed and the turning speed of No. 8 and the ambient air.

【0011】図2は図1の実施例の微粒化装置の噴霧特
性を示したものである。図中、A欄は液体供給部7が所
定の圧力で噴霧している状態をP1、噴霧が良好に行な
われる下限の圧力をP2、B欄は弁体13の開閉の状態
をON、OFFで示している。A=P1、B=ONの場
合は最良の噴霧状態で、噴霧量は最大で、粒子径も小さ
い。一般に液体供給部7の圧力を低下させると、噴霧状
態は悪化するが微粒化装置の使用目的に応じて、ある程
度調節は可能である。そのときの限界状態がA=P2、
B=ONであり、噴霧量は減少し、粒子径は少し大きく
なる。図5の従来例に示す圧力噴霧方式の微粒化装置は
この状態が限界であり、狭い範囲でしか調節ができなか
った。しかし、本実施例では、旋回導入路15a、15
bに各々別経路の液体供給管8a、8bと、弁体13を
設けているので、噴霧量の調節範囲を拡大することがで
きる。すなわち、A=P1、B=OFFの状態では、液
体は旋回導入路15aからのみ旋回室16に供給される
ので噴霧量は減少する。しかし、液体の供給圧力はP1
であり、旋回導入路15aから旋回室16に供給される
液体の流速はA=P1、B=ONの場合と同等なので、
旋回室16での液体の旋回状態、ひいては噴出孔17か
ら形成される液膜18の状態も等しくなり、噴霧状態も
良好で粒子径も同程度のものが得られる。同様にA=P
2、B=OFFの場合も噴霧量は減少するが、噴霧特性
はA=P2、B=ONの場合と同等の特性が得られる。
FIG. 2 shows the spray characteristics of the atomizing apparatus of the embodiment shown in FIG. In the figure, the column A indicates P1 when the liquid supply unit 7 is spraying at a predetermined pressure, the lower limit pressure P2 at which the spray is performed well, and the column B indicates whether the valve 13 is open or closed. Shows. When A = P1 and B = ON, the spraying state is the best, the spraying amount is maximum, and the particle size is also small. Generally, when the pressure of the liquid supply unit 7 is lowered, the atomized state deteriorates, but it can be adjusted to some extent according to the purpose of use of the atomizer. The limit state at that time is A = P2,
B = ON, the spray amount decreases, and the particle size increases a little. The pressure atomization type atomizer shown in the conventional example of FIG. 5 has a limit in this state and can be adjusted only in a narrow range. However, in the present embodiment, the turning introduction paths 15a, 15
Since the liquid supply pipes 8a and 8b and the valve body 13 each having different paths are provided in b, the adjustment range of the spray amount can be expanded. That is, in the state of A = P1 and B = OFF, the liquid is supplied to the swirl chamber 16 only from the swirl introduction passage 15a, so that the spray amount is reduced. However, the liquid supply pressure is P1
Since the flow velocity of the liquid supplied from the swirl introduction path 15a to the swirl chamber 16 is the same as when A = P1 and B = ON,
The swirling state of the liquid in the swirling chamber 16 and the state of the liquid film 18 formed from the ejection holes 17 are also equal, and the atomized state is good and the particle size is about the same. Similarly, A = P
Although the spray amount is also reduced when 2 and B = OFF, the spray characteristics are similar to those when A = P2 and B = ON.

【0012】図3は請求項2の液体微粒化装置の一実施
例を示したものである。図1の実施例と異なるのは、別
経路の液体供給管8a、8bに各々液体供給部19a、
(P A)、19b(PB)を設けている点である。この構
成により液体供給部19a、19bの圧力をP1からP2
までそれぞれ別個に設定することができるので、噴霧量
の調節範囲をさらに拡大することができる。
FIG. 3 shows an embodiment of the liquid atomizer of claim 2.
This is an example. The difference from the embodiment of FIG.
The liquid supply portions 19a, 19a are respectively connected to the liquid supply pipes 8a, 8b of the path.
(P A), 19b (PB) Is provided. This structure
The pressure of the liquid supply portions 19a and 19b from P1 to P2
Can be set separately up to
The adjustment range of can be further expanded.

【0013】図4は図3の実施例の微粒化装置の噴霧特
性を示したものである。図中、PA欄は液体供給部19
aの圧力の状態、PB欄は液体供給部19bの圧力の状
態をP1、P2、OFFで示している。図4からも明らか
なように、液体供給部19a、19bの圧力をP1から
P2までそれぞれ別個に設定することができるので、噴
霧量をQ5からQ8まで無段階に広範囲に調節することが
できる。圧力はP1からP2までの変動であり粒子径も噴
霧状態も安定した良好な状態が得られる。
FIG. 4 shows the spray characteristics of the atomizing apparatus of the embodiment shown in FIG. In the figure, the P A column is the liquid supply unit 19
The pressure state of "a" and the P B column show the pressure states of the liquid supply portion 19b by P1, P2, and OFF. As is apparent from FIG. 4, since the pressures of the liquid supply portions 19a and 19b can be set individually from P1 to P2, the spray amount can be adjusted in a wide range from Q5 to Q8 in a stepless manner. The pressure varies from P1 to P2, and a good state in which both the particle size and the spray state are stable can be obtained.

【0014】また、図1及び図2の実施例では説明を簡
単にするために旋回導入路および液体供給管が2本の場
合について説明したが、それぞれ2本以上であっても同
等もしくはそれ以上の効果が得られる。
Further, in the embodiment of FIGS. 1 and 2, the case where the swirl introduction path and the liquid supply pipe are two has been described for simplification of description, but even if each of them is two or more, they are equivalent or more. The effect of is obtained.

【0015】[0015]

【発明の効果】以上の説明から明らかなように請求項1
の液体微粒化装置は、旋回室に液体を導入する複数の旋
回導入路と、この旋回導入路に各々別経路から液体を供
給する液体供給管と、これら各々の液体供給管の経路に
設けられた弁体と、前記液体供給管に加圧状態で液体を
供給する液体供給部を有する構成としているので、弁体
の開閉によって旋回状態を一定に保ったまま旋回室に流
入する液体の量を調節することができ、噴霧状態や粒子
径が均一な状態で噴霧量の調節範囲を大きくとることが
できる。
As is apparent from the above description, claim 1
The liquid atomization device is provided with a plurality of swirl introduction paths for introducing the liquid into the swirl chamber, a liquid supply pipe for supplying the liquid to the swirl introduction path from different paths, and a path for each of these liquid supply pipes. Since the valve body and the liquid supply section for supplying the liquid to the liquid supply pipe under pressure are provided, the amount of the liquid flowing into the swirl chamber can be controlled by keeping the swirl state constant by opening and closing the valve body. It can be adjusted, and a large adjustment range of the spray amount can be taken in a sprayed state or a state where the particle size is uniform.

【0016】また、請求項2の液体微粒化装置は、旋回
室に液体を導入する複数の旋回導入路と、この旋回導入
路に各々別経路から液体を供給する液体供給管と、この
液体供給管にそれぞれ加圧状態で液体を供給する液体供
給部を有する構成としているので、液体供給管への液体
の供給圧力を各々独立して調節して噴霧量の細かな調節
ができるとともに、噴霧量の調節範囲をさらに大きくと
ることができる。
Further, in the liquid atomizing apparatus according to a second aspect of the invention, a plurality of swirl introducing passages for introducing the liquid into the swirl chamber, a liquid supply pipe for supplying the liquid to the swirl introducing passages from different routes, and the liquid supply Since each pipe is equipped with a liquid supply unit that supplies liquid in a pressurized state, the liquid supply pressure to the liquid supply pipes can be independently adjusted to finely adjust the spray amount, and also the spray amount. The adjustment range of can be made larger.

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

【図1】本発明の請求項1の一実施例における液体微粒
化装置の要部断面図
FIG. 1 is a sectional view of an essential part of a liquid atomizer according to an embodiment of claim 1 of the present invention.

【図2】同装置の特性図FIG. 2 is a characteristic diagram of the device.

【図3】本発明の請求項2の一実施例における液体微粒
化装置の要部断面図
FIG. 3 is a cross-sectional view of an essential part of a liquid atomizer according to an embodiment of claim 2 of the present invention.

【図4】同装置の特性図FIG. 4 is a characteristic diagram of the device.

【図5】従来の液体燃料燃焼装置の要部断面図FIG. 5 is a sectional view of a main part of a conventional liquid fuel combustion device.

【符号の説明】[Explanation of symbols]

7 液体供給部 8 液体供給管 13 弁体 15 旋回導入路 16 旋回室 17 噴出孔 7 Liquid Supply Section 8 Liquid Supply Pipe 13 Valve Body 15 Swirling Introduction Path 16 Swirling Chamber 17 Jet Hole

───────────────────────────────────────────────────── フロントページの続き (72)発明者 肆矢 規夫 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Norio Nobuya 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】液体が充填される旋回室と、この旋回室下
流側に設けられた噴出孔と、前記旋回室に旋回流れを発
生させるように液体を導入する複数の旋回導入路と、こ
の旋回導入路に各々別経路から液体を供給する液体供給
管と、前記各々の液体供給管の経路に設けられた弁体
と、前記液体供給管に加圧状態で液体を供給する液体供
給部を有する液体微粒化装置。
1. A swirl chamber filled with liquid, jet holes provided on the downstream side of the swirl chamber, a plurality of swirl introduction passages for introducing liquid so as to generate a swirl flow in the swirl chamber, A liquid supply pipe that supplies liquid to the swirl introduction passage from different routes, a valve body provided in the route of each of the liquid supply pipes, and a liquid supply unit that supplies liquid to the liquid supply pipe in a pressurized state. Liquid atomizer having.
【請求項2】液体が充填される旋回室と、この旋回室下
流側に設けられた噴出孔と、前記旋回室に旋回流れを発
生させるように液体を導入する複数の旋回導入路と、こ
の旋回導入路に各々別経路から液体を供給する液体供給
管と、前記各々の液体供給管に設けられ、加圧状態で液
体を供給する複数個の液体供給部を有する液体微粒化装
置。
2. A swirl chamber filled with liquid, jet holes provided on the downstream side of the swirl chamber, a plurality of swirl introduction passages for introducing liquid so as to generate a swirl flow in the swirl chamber, A liquid atomization device having a liquid supply pipe for supplying liquid to each of the swirl introduction passages from a different route, and a plurality of liquid supply units provided in each of the liquid supply pipes for supplying liquid in a pressurized state.
JP20930093A 1993-08-24 1993-08-24 Liquid atomizer Pending JPH0760170A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20930093A JPH0760170A (en) 1993-08-24 1993-08-24 Liquid atomizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20930093A JPH0760170A (en) 1993-08-24 1993-08-24 Liquid atomizer

Publications (1)

Publication Number Publication Date
JPH0760170A true JPH0760170A (en) 1995-03-07

Family

ID=16570674

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20930093A Pending JPH0760170A (en) 1993-08-24 1993-08-24 Liquid atomizer

Country Status (1)

Country Link
JP (1) JPH0760170A (en)

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