JP3517646B2 - Humidifier and method for subdividing bubbles in humidifier - Google Patents

Humidifier and method for subdividing bubbles in humidifier

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Publication number
JP3517646B2
JP3517646B2 JP2001036478A JP2001036478A JP3517646B2 JP 3517646 B2 JP3517646 B2 JP 3517646B2 JP 2001036478 A JP2001036478 A JP 2001036478A JP 2001036478 A JP2001036478 A JP 2001036478A JP 3517646 B2 JP3517646 B2 JP 3517646B2
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JP
Japan
Prior art keywords
bubbles
water
humidifier
layer
compressed air
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.)
Expired - Fee Related
Application number
JP2001036478A
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Japanese (ja)
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JP2002243220A (en
Inventor
一幸 橋本
恵介 窪田
伸二 佐々木
シー.アリ リチャード
アール.スチュワート トーマス
Original Assignee
株式会社 東京ウエルズ
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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】本発明は加湿器と、加湿器に
おける気泡の細分方法とに関し、特に水中に圧縮空気を
噴出し、生じた気泡を利用して加湿する加湿器と、この
加湿器における気泡の細分方法とに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a humidifier and a method for subdividing air bubbles in the humidifier, and more particularly to a humidifier for ejecting compressed air into water and humidifying the air using the generated air bubbles. And a method for subdividing bubbles.

【0002】[0002]

【従来の技術】従来使用されている加湿器として、水を
加熱したり、超音波により水を振動させたりすることに
よって水面からの水蒸気の分離を促進する、いわゆる高
濃度型の加湿器と、水中に圧縮空気を噴出して気泡を発
生させ、その気泡が水面に到達するまでに気泡中に水蒸
気を取り込む、いわゆる中濃度型の加湿器とがある。本
発明は後者の中濃度型の加湿器に関する。
2. Description of the Related Art As a conventional humidifier, a so-called high-concentration humidifier that promotes separation of water vapor from the water surface by heating water or vibrating the water with ultrasonic waves, There is a so-called middle-concentration type humidifier that ejects compressed air into water to generate bubbles and takes water vapor into the bubbles before the bubbles reach the water surface. The present invention relates to the latter medium concentration type humidifier.

【0003】従来の中濃度型の加湿器20は、断面状態
の図5を参照すると、水を収容する水溜1と、水溜1の
底部に配置した、相当数の貫通孔を有するパイプからな
る圧縮空気噴出手段2とを備える。パイプ2の貫通孔か
ら圧縮空気を噴出して気泡8を発生させると、気泡8は
水面4に向けて水中を上昇し、その上昇の間に水蒸気を
取り込む。気泡8が水面4に到達すると、気泡8から蒸
気溜り6に向けて水蒸気が放出される。水蒸気はその
後、蒸気溜り6から加湿器の放出口9を経て大気中に放
出され、大気を加湿する。
A conventional medium-concentration humidifier 20 has a cross section, as shown in FIG. 5, which comprises a water reservoir 1 for accommodating water and a pipe having a considerable number of through holes arranged at the bottom of the water reservoir 1. The air ejection means 2 is provided. When compressed air is ejected from the through hole of the pipe 2 to generate bubbles 8, the bubbles 8 rise in water toward the water surface 4 and take in water vapor during the rise. When the bubbles 8 reach the water surface 4, water vapor is released from the bubbles 8 toward the vapor pool 6. The water vapor is then released from the vapor reservoir 6 into the atmosphere through the outlet 9 of the humidifier to humidify the atmosphere.

【0004】[0004]

【発明が解決しようとする課題】加湿効果を高めるため
には、可能な限り多量に水蒸気を気泡8中に取り込ませ
なければならない。そのため、気泡が水と接触する時間
を長くすると共に、気泡8を小さくして表面積を大きく
する必要がある。ところが、気泡8は水中に噴出される
とほぼ鉛直に上昇することから、水との接触時間は水溜
1の高さによって限られている。
In order to enhance the moisturizing effect, it is necessary to incorporate as much water vapor into the bubbles 8 as possible. Therefore, it is necessary to increase the time during which the bubbles come into contact with water, and to reduce the size of the bubbles 8 to increase the surface area. However, since the bubbles 8 rise almost vertically when ejected into water, the contact time with water is limited by the height of the water reservoir 1.

【0005】一方、パイプ2にスポンジのような多孔質
体7を取り付け、貫通孔を覆っている。これによって、
噴出直後の気泡8を小さくしている。しかし、気泡8の
大きさは、水圧が高いと小さくなる性質を有するため、
噴出直後の小さい気泡8は、上昇するにつれて次第に大
きくなり、水面4近くでは気泡8aのように大きく膨張
してしまうことと、水圧が高い水溜1の底部では水蒸気
が蒸発し難いため、気泡内への水蒸気の取り込みは水面
4に近いほど良くなることから、気泡8を小さくして
も、実際には、気泡8に取り込まれる水蒸気の量は少な
い。加えて、気泡8が大きくなるつれて、気泡8に働く
浮力が増大し、気泡8の上昇速度が速まるため、気泡8
が水と接触する時間が短くなってしまい、この点からも
水蒸気の取り込み量が少なくなっている。
On the other hand, a porous body 7 such as a sponge is attached to the pipe 2 to cover the through hole. by this,
The bubble 8 immediately after the jet is made small. However, since the size of the bubble 8 has the property of becoming smaller when the water pressure is high,
The small bubbles 8 immediately after jetting gradually become larger as they rise, and expand greatly like the bubbles 8a near the water surface 4, and since the water vapor is difficult to evaporate at the bottom of the water reservoir 1 where the water pressure is high, it enters the bubbles. Since the amount of water vapor taken in is better as it gets closer to the water surface 4, even if the bubble 8 is made smaller, the amount of water vapor taken in the bubble 8 is actually small. In addition, as the bubble 8 becomes larger, the buoyancy acting on the bubble 8 increases and the rising speed of the bubble 8 increases, so that the bubble 8
The contact time with water becomes short, and the amount of water vapor taken in is also small from this point.

【0006】本発明は前記した問題点に鑑みてなされた
もので、その目的とするところは、限られた高さの水溜
において気泡の水との接触時間を長くすることができ、
水面近くにおいても小さな気泡を与えることができる、
加湿器と、加湿器における気泡の細分方法とを提供する
ことにある。
The present invention has been made in view of the above problems, and an object of the present invention is to make it possible to prolong the contact time of bubbles with water in a water reservoir having a limited height.
Can give small bubbles even near the water surface,
A humidifier and a method for subdividing air bubbles in the humidifier.

【0007】[0007]

【課題を解決するための手段】前記課題を解決するた
め、本願発明は次の構成とした。請求項1記載の発明の
要旨は、水を収容する水溜と、この水溜の底部に配置さ
れる圧縮空気噴出手段と、前記圧縮空気噴出手段から噴
出され、水中を上昇する気泡の上昇経路に配置した気泡
細分層と、を有してなり、前記気泡細分層は、球形の粒
体を層状に配置した粒体層からなることを特徴とする加
湿器に存する。請求項2記載の発明の要旨は、前記粒体
の外径は、前記気泡の直径の約 6.4 倍以下の大きさであ
ることを特徴とする、請求項1に記載の加湿器に存す
る。請求項3記載の発明の要旨は、加湿器の水溜に収容
した水に噴出する圧縮空気の気泡を細分する方法であっ
て、前記気泡を球形の粒体を層状に配置した粒体層から
なる気泡細分層を経て上昇させることを特徴とする、加
湿器における気泡の細分方法に存する。
In order to solve the above problems, the present invention has the following structure. Summary of the Invention in a first aspect, a basin containing water, and compressed air injection means located at the bottom of the basin, is ejected from the compressed air injection means, disposed rise path of bubbles rising in water A cell subdivided layer, and the cell subdivided layer is a spherical particle.
An additional feature characterized by being composed of granular layers in which the bodies are arranged in layers.
Exists in a moisturizer . The gist of the invention according to claim 2 is the granular material.
The outer diameter of the bubble is about 6.4 times the diameter of the bubble or less.
It exists in the humidifier of Claim 1 characterized by the above-mentioned. The gist of the invention according to claim 3 is that it is housed in a water reservoir of a humidifier.
It is a method of subdividing the bubbles of compressed air that jets into
The bubbles from the granular layer in which spherical granular particles are arranged in layers.
It is characterized in that the
It lies in the method of subdividing air bubbles in a moisturizer.

【0008】[0008]

【発明の実施の形態】以下に本発明の実施形態を図面を
参照して説明する。図面中、従来の部品と実質的に同じ
機能を有する部品に同じ符号を付けてある。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. In the drawings, parts having substantially the same functions as those of conventional parts are designated by the same reference numerals.

【0009】加湿器10は、断面状態の図1と、水の上
昇経路を模式的に示す図2とを参照すると、水を収容す
る水溜1と、水溜1の底部に配置される圧縮空気噴出手
段2とを備える。
Referring to FIG. 1 in a sectional view and FIG. 2 schematically showing a rising path of water, the humidifier 10 has a water reservoir 1 for accommodating water and a jet of compressed air arranged at the bottom of the water reservoir 1. And means 2.

【0010】水溜1は頂部中央に蒸気の放出口9を有す
る。水溜1は、後述する圧縮空気噴出手段2や気泡細分
層3aを水溜1内に設置する際の便宜から、一般には、
上下に分けた2つの容器部分で形成し、2つの容器部分
をパッキンを介在して結合する形態とするが、図示で
は、一体のものとして示してある。
The water reservoir 1 has a steam outlet 9 at the center of the top. The water reservoir 1 is generally composed of a compressed air jetting means 2 and a bubble subdivision layer 3a, which will be described later, for the convenience of installation in the water reservoir 1.
Although it is formed by two container parts which are divided into an upper part and a lower part, and the two container parts are joined together with a packing interposed, they are shown as one body in the figure.

【0011】圧縮空気噴出手段2は、図示の実施形態で
は一端をふたしたパイプからなり、水溜1内に位置する
パイプ2の部分に相当数の貫通孔2aが開けられ、圧縮
空気の噴出口となっている。加湿器10の使用時には、
パイプ2の他端部をコンプレッサのような圧縮空気源
(図示せず)に接続する。パイプ2に、図5に示した多
孔質体7を取り付ける必要はない。
In the illustrated embodiment, the compressed air ejecting means 2 is composed of a pipe having one end covered, and a considerable number of through holes 2a are formed in the portion of the pipe 2 located in the water reservoir 1 to form a compressed air ejection port. Has become. When using the humidifier 10,
The other end of the pipe 2 is connected to a compressed air source (not shown) such as a compressor. It is not necessary to attach the porous body 7 shown in FIG. 5 to the pipe 2.

【0012】加湿器10は、圧縮空気噴出手段2から噴
出され、水中を上昇する気泡5aの上昇経路5bに配置
した気泡細分層3aを有する。図示の実施形態では、気
泡細分層3aは、実質的に同じ直径のガラス球3を層状
に配置した粒体層からなる。
The humidifier 10 has a bubble subdivision layer 3a arranged in a rising path 5b of bubbles 5a which are jetted from the compressed air jetting means 2 and rise in water. In the illustrated embodiment, the cell subdivision layer 3a is composed of a granular layer in which glass spheres 3 having substantially the same diameter are arranged in layers.

【0013】圧縮空気噴出手段2に圧縮空気を供給し、
貫通孔2aから圧縮空気を噴出させると、気泡5aが発
生する。この気泡5aは水面4に向けて上昇する間に、
上昇経路5bに配置した気泡細分層3aにあるガラス球
3相互間の細隙を通過し、いくつもの微細気泡5に分裂
する。このように分裂した微細気泡5は、その内部に水
蒸気を取り込む。水蒸気を取り込んだ微細気泡5は水面
4に到達すると、水蒸気を水蒸気溜り6に放出する。放
出された水蒸気は、水蒸気溜り6から水溜1の放出口9
を経て大気中に放出され、大気を加湿する。
Compressed air is supplied to the compressed air jetting means 2,
When compressed air is ejected from the through hole 2a, bubbles 5a are generated. While the bubbles 5a rise toward the water surface 4,
It passes through the slits between the glass spheres 3 in the bubble subdivision layer 3a arranged on the ascending path 5b, and is divided into a number of fine bubbles 5. The fine bubbles 5 thus split take in water vapor inside. When the fine bubbles 5 that have taken in the water vapor reach the water surface 4, they release the water vapor into the water vapor reservoir 6. The released water vapor is discharged from the water vapor reservoir 6 into the water outlet 1 of the water reservoir 1.
After being released into the atmosphere, it humidifies the atmosphere.

【0014】前述の説明から分かるように、気泡細分層
3aは、気泡5aが通過する細隙を作るものである。し
たがって、気泡細分層3aが粒体層からなる場合、粒体
層の個々の粒体は細隙を作ることができる形状であれ
ば、どのような形態でもよく、球形以外の多面体とする
こともできる。しかし、球の表面積が最小直径で最大と
なることから、粒体層の個々の粒体は球形であることが
好ましい。
As can be seen from the above description, the bubble subdivision layer 3a creates a slit through which the bubbles 5a pass. Therefore, when the cell subdivision layer 3a is formed of a granular layer, the individual particles of the granular layer may have any shape as long as they can form a slit, and may be a polyhedron other than a spherical shape. it can. However, it is preferred that the individual grains of the grain layer are spherical, as the surface area of the sphere will be greatest at the smallest diameter.

【0015】次に、模式的に示した図3及び図4を参照
して、微細気泡5ができる過程を説明する。図3に示す
ように、同じ半径r(直径d)のガラス球3が3個
接するとき、3個のガラス球3に囲まれた空間内で3個
のガラス球に接する円(半径r、直径d)は、水中
で空気がガラス球3の間を通過するとき、表面張力でで
きる球の断面と同じであり、 {(r+r)/r}=2/√3 の関係が成り立つ。したがって、 d={(2/√3)−1}d となる。これは、ガラス球3の直径dが定まると、微
細気泡5の直径dが定まることを意味する。
Next, the process of forming the fine bubbles 5 will be described with reference to FIGS. As shown in FIG. 3, when three glass spheres 3 having the same radius r 2 (diameter d 2 ) are in contact with each other, a circle (radius r which is in contact with the three glass spheres in a space surrounded by the three glass spheres 3 has a radius r 1 , the diameter d 1 ) is the same as the cross section of a sphere formed by surface tension when air passes between the glass spheres 3 in water, and {(r 1 + r 2 ) / r 2 } = 2 / √3 The relationship is established. Therefore, d 1 = {(2 / √3) -1} d 2 . This means that when the diameter d 2 of the glass sphere 3 is determined, the diameter d 1 of the fine bubbles 5 is determined.

【0016】次に、図4を参照して、ガラス球3,3間
の通過状態を説明する。大きな気泡5cがガラス球3,
3間を通過すると、直径dがガラス球3の直径d
{(2/√3)−1}倍の微細気泡5が発生し、上昇し
てゆく。上昇の過程で微細気泡5が膨張しても、ガラス
球3が層状に配置されているため、その層を通過し終わ
るまで、微細気泡5の直径dは実質的に同じである。
その結果、微細気泡5の直径dが小さい分、全体の表
面積が大きくなり、微細気泡5内に水蒸気を多く取り込
むことができる。加えて、気泡5aがガラス球3,3間
を通過するとき、図2に示すように、気泡5aは上向き
だけでなく左右の向きにも移動しながら微細気泡5とな
るため、全体の移動距離が長くなり、微細気泡5の水と
の接触時間が長くなる。この点からも、微細気泡5内へ
の水蒸気の取り込み量が多くなる。
Next, the passing state between the glass balls 3 will be described with reference to FIG. Large bubbles 5c are glass balls 3,
When passing through 3, the fine bubbles 5 having a diameter d 1 {(2 / √3) -1} times the diameter d 2 of the glass sphere 3 are generated and rise. Even if the fine bubbles 5 expand in the process of rising, since the glass spheres 3 are arranged in layers, the diameters d 1 of the fine bubbles 5 are substantially the same until they pass through the layer.
As a result, the smaller the diameter d 1 of the fine bubbles 5, the larger the total surface area, and the larger amount of water vapor can be taken into the fine bubbles 5. In addition, when the bubbles 5a pass between the glass balls 3 and 3, as shown in FIG. 2, the bubbles 5a become fine bubbles 5 while moving not only in the upward direction but also in the left and right directions. Becomes longer and the contact time of the fine bubbles 5 with water becomes longer. From this point as well, the amount of water vapor taken into the fine bubbles 5 increases.

【0017】前述したところから明らかであるように、
圧縮空気噴出手段2の貫通孔2aから噴出した気泡5a
の直径が、3個のガラス球3に囲まれた空間内で3個の
ガラス球3に接する円の直径d以上であるとき、気泡
5aが分裂して微細気泡5となってゆくため、1つの気
泡5aから複数の微細気泡5を発生させることができ
る。このようにして生じた微細気泡5は、層状に配置さ
れたガラス球3,3間の細隙を通過し終わるまで、実質
的に一定の直径dに保たれる。
As is apparent from the above,
Bubbles 5a ejected from the through holes 2a of the compressed air ejection means 2
When the diameter of is greater than or equal to the diameter d 1 of the circle that is in contact with the three glass spheres 3 in the space surrounded by the three glass spheres 3, the bubbles 5a are divided and become the fine bubbles 5, It is possible to generate a plurality of fine bubbles 5 from one bubble 5a. The fine bubbles 5 generated in this way are kept at a substantially constant diameter d 1 until they have passed through the narrow gap between the glass balls 3, 3 arranged in layers.

【0018】逆に、圧縮空気噴出手段2の貫通孔2aか
ら噴出した気泡5aの直径が、3個のガラス球3に囲ま
れた空間内で3個のガラス球3に接する円の直径d
り小さいとき、気泡5aはガラス球3,3間の細隙を素
通りしてしまう。この状態では、気泡5aが分裂するこ
とによる微細気泡5の発生はない。ガラス球3,3間を
素通りした気泡5aは、上昇経路5bを上昇する間に水
圧が低くなるにつれて次第に体積が膨張してゆくことか
ら、ある上昇位置で直径がd以上になる。そうする
と、前述したところに従って分裂し、微細気泡5とな
る。
On the contrary, the diameter of the bubble 5a ejected from the through hole 2a of the compressed air ejecting means 2 is the diameter d 1 of the circle which is in contact with the three glass spheres 3 in the space surrounded by the three glass spheres 3. When it is smaller, the bubbles 5a pass through the narrow gaps between the glass balls 3 and 3. In this state, the fine bubbles 5 are not generated due to the splitting of the bubbles 5a. The bubble 5a passing through between the glass balls 3 and 3 gradually expands in volume as the water pressure decreases while rising along the ascending path 5b, so that the diameter becomes d 1 or more at a certain ascending position. Then, the cells are split according to the above-mentioned points to form the fine bubbles 5.

【0019】微細気泡5の直径dとガラス球3の直径
との関係を示す前記式は、ガラス球3の直径d
微細気泡5の直径dによって制限されることを示して
いる。すなわち、d≒6.4dとなることから、ガラ
ス球3の直径dを微細気泡5の直径dの約6.4倍以
下に定めることが好ましい。これによって、水蒸気の取
り込みの多い微細気泡5が得られることととなる。
[0019] The expression that indicates the relationship between the diameter d 2 of the diameter d 1 and the glass bulb 3 of fine bubbles 5, shows that the diameter d 2 of the glass bulb 3 is restricted by the diameter d 1 of the fine bubbles 5 There is. That is, since d 2 ≈6.4d 1 , the diameter d 2 of the glass sphere 3 is preferably set to about 6.4 times the diameter d 1 of the fine bubbles 5 or less. As a result, the fine bubbles 5 having a large intake of water vapor can be obtained.

【0020】本発明に係る圧縮空気の気泡を細分する方
法は、再び図1及び図2を参照すると、加湿器10の水
溜1に収容した水に噴出する圧縮空気の気泡5aを細分
するものであり、気泡5aを気泡細分層3aを経て上昇
させる。そうすると、気泡細分層3aで小さくされた微
細気泡5が得られる。
Referring to FIGS. 1 and 2 again, the method of subdividing the compressed air bubbles according to the present invention is to subdivide the compressed air bubbles 5a ejected into the water stored in the water reservoir 1 of the humidifier 10. Yes, the bubbles 5a are raised through the bubble subdivision layer 3a. Then, the fine bubbles 5 reduced in the bubble subdivision layer 3a are obtained.

【0021】前記実施形態では、気泡細分層3aは粒体
層であり、粒体層中の粒体はガラス球3であった。粒体
層中の粒体として、セラミック球やプラスチック球、ア
ルミ球のような、水に対して不活性な物体を選ぶことが
できる。また、気泡細分層3aとして、円筒柱や多角形
柱のような筒体層を使用することができる。すなわち、
図1の紙面に垂直な方向へ筒体の軸線が伸びるように、
相当数の筒体を水溜1内に配置して気泡細分層3aとす
る。
In the above-mentioned embodiment, the cell subdivision layer 3a is a particle layer, and the particles in the particle layer are the glass spheres 3. As the particles in the particle layer, it is possible to select a substance that is inert to water, such as a ceramic sphere, a plastic sphere, or an aluminum sphere. Further, as the cell subdivision layer 3a, a cylindrical body layer such as a cylindrical column or a polygonal column can be used. That is,
1 so that the axis of the cylinder extends in a direction perpendicular to the paper surface of FIG.
A considerable number of cylinders are arranged in the water reservoir 1 to form the cell subdivision layer 3a.

【0022】気泡細分層3aの高さ、つまり微細気泡5
を得ることができる範囲は、適当な大きさの微細気泡5
が得られる限り、任意に選定できる。
The height of the bubble subdivision layer 3a, that is, the fine bubbles 5
The range that can obtain the
Can be arbitrarily selected as long as

【0023】[0023]

【発明の効果】本発明によれば、圧縮空気噴出手段から
噴出された気泡が微細気泡になることと、気泡細分層を
通過する間、微細気泡が実質的に同じ大きさに保たれる
ことから、水との接触面積が大きくなり、より多くの水
蒸気を取り込むことができる。また、微細気泡となって
上昇するとき、上向きだけでなく、左右の向きにも移動
するため、微細気泡の移動時間が長くなり、この点から
もより多くの水蒸気を取り込むことができる。その結
果、加湿器から放出される水蒸気量を増やし、加湿効果
を高めることができる。
According to the present invention, the bubbles ejected from the compressed air ejecting means become fine bubbles and the fine bubbles are kept substantially the same size while passing through the bubble subdivision layer. Therefore, the contact area with water becomes large, and more water vapor can be taken in. Further, when rising as fine bubbles, the fine bubbles move not only in the upward direction but also in the left and right directions, so that the moving time of the fine bubbles becomes long, and from this point, more water vapor can be taken in. As a result, the amount of water vapor released from the humidifier can be increased and the humidifying effect can be enhanced.

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

【図1】本発明に係る加湿器の実施形態を示す断面図で
ある。
FIG. 1 is a sectional view showing an embodiment of a humidifier according to the present invention.

【図2】気泡の上昇経路を示す模式図である。FIG. 2 is a schematic diagram showing a rising path of bubbles.

【図3】微細気泡の理論的な大きさを示す模式図であ
る。
FIG. 3 is a schematic diagram showing a theoretical size of fine bubbles.

【図4】気泡が微細気泡となって2つのガラス球の間を
通過する状態を示す模式図である。
FIG. 4 is a schematic view showing a state in which bubbles become fine bubbles and pass between two glass balls.

【図5】従来の加湿器を示す断面図である。FIG. 5 is a cross-sectional view showing a conventional humidifier.

【符号の説明】[Explanation of symbols]

1 水溜 2 圧縮空気噴出手段 2a 貫通孔 3 ガラス球 3a 気泡細分層 4 水面 5 微細気泡 5a 気泡 5b 上昇経路 5c 大きな気泡 6 水蒸気溜り 7 多孔質体 8 気泡 8a 気泡 9 放出口 10 本発明に係る加湿器 20 従来の加湿器 1 pool 2 Compressed air ejection means 2a through hole 3 glass balls 3a Cell subdivision layer 4 water surface 5 Micro bubbles 5a bubbles 5b climbing path 5c big bubbles 6 Steam pool 7 Porous body 8 bubbles 8a bubbles 9 outlet 10 Humidifier according to the present invention 20 Conventional humidifier

───────────────────────────────────────────────────── フロントページの続き (72)発明者 リチャード シー.アリ アメリカ合衆国 カリフォルニア州 95076,ワトソンビレ ウエストリッジ ドライブ 200 シエラサーモプロダ クション ファーネス インコーポレー テッド内 (72)発明者 トーマス アール.スチュワート アメリカ合衆国 カリフォルニア州 95076,ワトソンビレ ウエストリッジ ドライブ 200 シエラサーモプロダ クション ファーネス インコーポレー テッド内 (56)参考文献 特開 平10−201847(JP,A) 特開 平9−70435(JP,A) 特開 平8−24606(JP,A) (58)調査した分野(Int.Cl.7,DB名) F24F 6/00 - 6/18 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Richard C. Ali United States California 95076 Watsonville Westridge Drive 200 Sierra Thermo Productions Furnace Incorporated (72) Inventor Thomas Earl. Stewart United States California 95076 Watsonville Westridge Drive 200 Sierra Thermo Productions in Furnace Incorporated (56) References JP 10-201847 (JP, A) JP 9-70435 (JP, A) JP JP 8-24606 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) F24F 6/00-6/18

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水を収容する水溜と、 この水溜の底部に配置される圧縮空気噴出手段と、 前記圧縮空気噴出手段から噴出され、水中を上昇する気
泡の上昇経路に配置した気泡細分層と、を有してなり、 前記気泡細分層は、球形の粒体を層状に配置した粒体層
からなることを特徴とする加湿器。
1. A water reservoir for containing water, a compressed air ejection means arranged at the bottom of the water reservoir, and an air bubble subdivided layer arranged in an ascending path of bubbles emanating from the compressed air ejection device and rising in water. And the cell subdivision layer is a particle layer in which spherical particles are arranged in layers.
A humidifier characterized by comprising.
【請求項2】 前記粒体の外径は、前記気泡の直径の約
6.4 倍以下の大きさであることを特徴とする、請求項1
に記載の加湿器。
2. The outer diameter of the granules is about the diameter of the bubbles.
6. The size is 6.4 times or less, and the size is 1.
Humidifier described in.
【請求項3】 加湿器の水溜に収容した水に噴出する圧
縮空気の気泡を細分する方法であって、 前記気泡を球形の粒体を層状に配置した粒体層からなる
気泡細分層を経て上昇させることを特徴とする、加湿器
における気泡の細分方法。
3. The pressure that is jetted into the water stored in the water reservoir of the humidifier.
A method for subdividing air bubbles of condensed air, which comprises a particle layer in which spherical particles are arranged in layers.
Humidifier characterized by rising through a cell subdivision layer
Method for subdividing bubbles in.
JP2001036478A 2001-02-14 2001-02-14 Humidifier and method for subdividing bubbles in humidifier Expired - Fee Related JP3517646B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001036478A JP3517646B2 (en) 2001-02-14 2001-02-14 Humidifier and method for subdividing bubbles in humidifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001036478A JP3517646B2 (en) 2001-02-14 2001-02-14 Humidifier and method for subdividing bubbles in humidifier

Publications (2)

Publication Number Publication Date
JP2002243220A JP2002243220A (en) 2002-08-28
JP3517646B2 true JP3517646B2 (en) 2004-04-12

Family

ID=18899746

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Country Link
JP (1) JP3517646B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6267142B2 (en) * 2015-03-05 2018-01-24 ヤフー株式会社 Air conditioning system, building and data center
TWI564525B (en) * 2015-05-07 2017-01-01 Wei Yi Chiang Energy saving method and device for direct heat recovery
JP2018036046A (en) * 2017-10-06 2018-03-08 ヤフー株式会社 Air conditioning system, building and data center
JP7424791B2 (en) 2019-10-25 2024-01-30 日本ボールドウィン株式会社 Drying control device for roller surface

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