JP5287567B2 - Liquid refinement device and sauna device using the same - Google Patents

Liquid refinement device and sauna device using the same Download PDF

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JP5287567B2
JP5287567B2 JP2009167413A JP2009167413A JP5287567B2 JP 5287567 B2 JP5287567 B2 JP 5287567B2 JP 2009167413 A JP2009167413 A JP 2009167413A JP 2009167413 A JP2009167413 A JP 2009167413A JP 5287567 B2 JP5287567 B2 JP 5287567B2
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liquid
water
rotating plate
exhaust port
refinement
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JP2011021816A (en
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和大 齋藤
広幸 近藤
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Panasonic Corp
Panasonic Holdings Corp
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Panasonic Corp
Matsushita Electric Industrial Co Ltd
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Priority to CN2009801349110A priority patent/CN102144133B/en
Priority to PCT/JP2009/004430 priority patent/WO2010029722A1/en
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Priority to HK11109990.8A priority patent/HK1155797A1/en
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Abstract

<P>PROBLEM TO BE SOLVED: To eliminate execution of piping work for discharging unrefined liquid, and to simplify work execution, in a liquid refining device and a sauna device using the same. <P>SOLUTION: The liquid refining device includes: a heat exchanger 7 and a fan motor 8a provided on an air course connecting a suction port 4 with an exhaust port 5; and a liquid refining means 9 provided between the fan motor 8a and the exhaust port 5. The liquid refining means 9 is constituted of a rotating means 13 and a liquid supply means for supplying liquid to the rotating means 13. The liquid supply means has: an upper supply means for supplying liquid to an upper rotating plate 16a; and a lower supply means for supplying liquid to a lower rotating plate 16b. The lower supply means has: a water storage means 19; and a water passage 20 for supplying liquid from the water storage means 19 to the lower rotating plate 16b. The liquid supply position from the water passage 20 to the lower rotating plate 16b is arranged on the outer side from the liquid supply position to the upper rotating plate 16a. A heat exchanger 10 for an auxiliary heating means is provided between the liquid refining means 9 and the exhaust port 5 as the auxiliary heating means. <P>COPYRIGHT: (C)2011,JPO&amp;INPIT

Description

本発明は、液体微細化装置とそれを用いたサウナ装置に関するものである。   The present invention relates to a liquid miniaturization apparatus and a sauna apparatus using the same.

例えば、サウナ装置に用いられる液体微細化装置の構成は、次のような構成となっていた。   For example, the configuration of a liquid micronizer used for a sauna device has the following configuration.

すなわち、吸込口と排気口を有する本体ケースと、この本体ケース内の通気路に設けた加熱手段および送風手段と、この送風手段と排気口間に設けた微細化手段とを備え、前記微細化手段は、給水管から液体を噴射させる構成となっていた(例えば特許文献1参照)。   That is, a main body case having a suction port and an exhaust port, a heating unit and a blower unit provided in a ventilation path in the main body case, and a miniaturization unit provided between the blower unit and the exhaust port, The means is configured to eject liquid from the water supply pipe (see, for example, Patent Document 1).

特開平6−63103号公報JP-A-6-63103

上記従来例で課題となるのは、ノズルから噴出された液体のうち、微細化できなかった液体を排出するために、サウナ室に配管を施工しなければならず、施工作業が煩雑になるということである。   The problem with the above conventional example is that, in order to discharge the liquid ejected from the nozzle that could not be refined, piping must be constructed in the sauna room, which makes the construction work complicated. That is.

すなわち、ノズルから液体を噴出して液体を微細化するタイプのものでは、液体を完全に微細化することができず、サウナ装置に残った大量の非微細化液体を処理するためにサウナ室に配管を延長して、この非微細化液体をサウナ室に排出するようになっている。このような配管をサウナ室に美観的に施工するのは非常に煩雑な作業となっている。   That is, in the type in which the liquid is ejected from the nozzle and the liquid is refined, the liquid cannot be completely refined, and in the sauna room in order to process a large amount of non-miniaturized liquid remaining in the sauna apparatus. The pipe is extended to discharge this non-fine liquid to the sauna room. It is very troublesome to construct such a pipe in the sauna room aesthetically.

そこで本発明は、施工作業を簡単に行えるようにすることを目的とするものである。   Therefore, an object of the present invention is to facilitate construction work.

そして、この目的を達成するために本発明は、吸込口と排気口を有する本体ケースと、この本体ケース内の前記吸込口と前記排気口を結ぶ風路に設けた加熱手段および送風手段と、この送風手段と前記排気口間の風路内に設けた液体微細化手段とを備え、前記液体微細化手段は、上下方向に開口した筒状の経路と、この筒状の経路内に設けた回転手段と、この回転手段に液体を供給する液体供給手段とを有し、前記回転手段は、上下方向に向けて配置した回転軸と、この回転軸の軸方向に所定間隔で固定した複数の回転板とを有し、前記液体供給手段は、上方の回転板に液体を供給する上供給手段と、下方の回転板に液体を供給する下供給手段とを有し、この下供給手段は、前記筒状の経路の内壁に設けた貯水手段と、この貯水手段から下方の回転板へ液体を供給する水路とを有し、この水路から下方の回転板への液体供給位置は、上方の回転板への液体供給位置より外側に配置し、補助加熱手段を前記液体微細化手段と前記排気口との間に設けた構成とし、これにより、上記目的を達成している。   And in order to achieve this object, the present invention comprises a main body case having a suction port and an exhaust port, a heating unit and a blower unit provided in an air passage connecting the suction port and the exhaust port in the main body case, A liquid refining means provided in the air passage between the blower means and the exhaust port, and the liquid refining means is provided in a cylindrical path opened in a vertical direction and in the cylindrical path. A rotating means, and a liquid supply means for supplying a liquid to the rotating means. The rotating means includes a rotating shaft arranged in the vertical direction and a plurality of shafts fixed at predetermined intervals in the axial direction of the rotating shaft. The liquid supply means includes an upper supply means for supplying liquid to the upper rotary plate, and a lower supply means for supplying liquid to the lower rotary plate. Water storage means provided on the inner wall of the cylindrical path, and downward from the water storage means A liquid channel for supplying liquid to the rotating plate, the liquid supply position from the water channel to the lower rotating plate is arranged outside the liquid supplying position to the upper rotating plate, and the auxiliary heating means The structure is provided between the means and the exhaust port, thereby achieving the above object.

以上のように、本発明は、液体微細化を、回転手段と、この回転手段に液体を供給する液体供給手段と、補助加熱手段を液体微細化手段と排気口との間に設けた構成にすることにより、高速で回転する回転手段に微細化に必要な最低限の液体を供給して液体を微細化し、微細化しきれなかった液体は、補助加熱手段にて気化させるので、結果として、液体の微細化時に大量の排液が発生しないものとなる。   As described above, the present invention has a configuration in which the liquid refinement is provided by the rotation means, the liquid supply means for supplying the liquid to the rotation means, and the auxiliary heating means between the liquid refinement means and the exhaust port. By supplying the minimum liquid necessary for miniaturization to the rotating means that rotates at high speed, the liquid is refined, and the liquid that has not been miniaturized is vaporized by the auxiliary heating means. A large amount of drainage does not occur during the refinement of the material.

つまり、微細化終了時においては、供給した液体をほぼすべて微細化あるいは気化することができ、その結果として、施工作業が簡単になるという効果を奏する。   That is, at the end of miniaturization, almost all of the supplied liquid can be miniaturized or vaporized, and as a result, the construction work can be simplified.

しかも、液体供給手段は、上方の回転板に液体を供給する上供給手段と、下方の回転板に液体を供給する下供給手段とを有し、この下供給手段は、前記筒状の経路の内壁に設けた貯水手段と、この貯水手段から下方の回転板へ液体を供給する水路とを有し、この水路から下方の回転板への液体供給位置は、上方の回転板への液体供給位置より外側である構成とすることにより、水路が短くなるため、回転板の間隔を小さくでき、回転板の数量を増やしても液体微細化装置の小型化が実現できる。   In addition, the liquid supply means has an upper supply means for supplying liquid to the upper rotating plate and a lower supply means for supplying liquid to the lower rotating plate, and the lower supply means has the cylindrical path. A water storage means provided on the inner wall and a water channel for supplying liquid from the water storage means to the lower rotating plate, the liquid supply position from the water path to the lower rotating plate is the liquid supply position to the upper rotating plate. Since the water channel is shortened by adopting an outer configuration, the interval between the rotating plates can be reduced, and the liquid miniaturization apparatus can be downsized even if the number of rotating plates is increased.

本発明の実施の形態における液体微細化装置を用いたサウナ装置の斜視図The perspective view of the sauna apparatus using the liquid refinement | miniaturization apparatus in embodiment of this invention 同液体微細化装置の垂直断面の構成図Configuration diagram of the vertical cross section of the same liquid micronizer (a)同液体微細化装置の内部(加湿用風路)の斜視図、(b)同液体微細化装置の内部(加熱用風路)の斜視図(A) Perspective view of the inside of the liquid micronizer (humidification air channel), (b) Perspective view of the inside of the liquid micronizer (air channel for heating) 同液体微細化手段の垂直断面の構成図Configuration diagram of vertical cross section of the same liquid refinement means 同液体微細化手段の供給手段の斜視図The perspective view of the supply means of the liquid refinement means 同液体微細化手段の構成を示す斜視図The perspective view which shows the structure of the liquid refinement | miniaturization means 同液体微細化手段と補助加熱手段との位置関係を示す垂直断面の構成図Configuration diagram of vertical section showing the positional relationship between the liquid refinement means and the auxiliary heating means

以下、本発明の実施の形態について、図面を参照しながら説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

(実施の形態)
図1は、本発明の実施の形態における液体微細化装置を用いたサウナ装置の斜視図であり、この図1に示すように、サウナ室1の天井面2には、液体微細化装置3が取り付けられている。
(Embodiment)
FIG. 1 is a perspective view of a sauna apparatus using a liquid micronizer according to an embodiment of the present invention. As shown in FIG. 1, a liquid micronizer 3 is provided on a ceiling surface 2 of a sauna room 1. It is attached.

図2は、本発明の実施の形態における液体微細化装置の垂直断面の構成図、図3は、同内部の斜視図、図4は、同液体微細化手段の垂直断面の構成図、図5は、同液体微細化手段の供給手段の斜視図、図6は、同液体供給手段の構成を示す斜視図、図7は、同液体微細化手段と補助加熱手段との位置関係を示す垂直断面の構成図である。   2 is a configuration diagram of a vertical cross section of the liquid micronization apparatus in the embodiment of the present invention, FIG. 3 is a perspective view of the inside thereof, FIG. 4 is a configuration diagram of a vertical cross section of the liquid micronization means, FIG. Is a perspective view of the supply means of the liquid refinement means, FIG. 6 is a perspective view showing the configuration of the liquid supply means, and FIG. 7 is a vertical cross section showing the positional relationship between the liquid refinement means and the auxiliary heating means FIG.

液体微細化装置3は、図2と図3に示すように、吸込口4と排気口5を有する本体ケース6と、この本体ケース6内の吸込口4と排気口5とを結ぶ風路の吸込口4の近傍に設けた加熱手段としての加熱手段用の熱交換器7および送風手段としてのファンモータ8aと、このファンモータ8aと排気口5との間に、液体微細化手段9と、図7に示すように、この液体微細化手段9と排気口5との間に補助加熱手段としての補助加熱手段用の熱交換器10とを備えた構成としている。   As shown in FIGS. 2 and 3, the liquid micronizer 3 has a main body case 6 having a suction port 4 and an exhaust port 5, and an air passage connecting the suction port 4 and the exhaust port 5 in the main body case 6. A heat exchanger 7 for a heating means as a heating means provided in the vicinity of the suction port 4 and a fan motor 8a as a blowing means, and between the fan motor 8a and the exhaust port 5, a liquid refinement means 9; As shown in FIG. 7, a heat exchanger 10 for auxiliary heating means as auxiliary heating means is provided between the liquid micronizing means 9 and the exhaust port 5.

なお、本実施の形態では、一例として、吸込口4と排気口5とを結ぶ風路は、吸込口4から加熱手段用の熱交換器7を通過後、図3(a)に示す、液体微細化手段9を経由する加湿用の風路(矢印A)と、図3(b)に示す、液体微細化手段9を経由しない加熱用の風路(矢印B)の2風路に分岐した構成としている。   In the present embodiment, as an example, the air path connecting the suction port 4 and the exhaust port 5 passes through the heat exchanger 7 for heating means from the suction port 4 and then the liquid shown in FIG. The air is branched into two air paths, a humidifying air passage (arrow A) passing through the finer means 9 and a heating air passage (arrow B) not passing through the liquid refining means 9 shown in FIG. It is configured.

まず、加湿用の風路(矢印A)構成から説明する。   First, the configuration of the air path for humidification (arrow A) will be described.

図2に示すように、ファンモータ8aから液体微細化手段9へ通じる風路は、ケーシング10aとダクト11aにより形成されており、矢印Aに示すように、筒状の経路12の下側開口に接続している。   As shown in FIG. 2, the air passage leading from the fan motor 8a to the liquid micronization means 9 is formed by the casing 10a and the duct 11a, and as shown by the arrow A, in the lower opening of the cylindrical path 12 Connected.

そして、液体微細化手段9は、吸込口4と排気口5とを結ぶ風路(加湿用の風路)内の筒状の経路12と、この筒状の経路12の内部に設けた回転手段13と、この回転手段13に液体を供給する液体供給手段として、上方の回転板16aに液体を供給する上供給手段としての給水管14、下方の回転板16bに液体を供給する下供給手段18とを有している。   The liquid micronization means 9 includes a cylindrical path 12 in an air path (humidification air path) connecting the suction port 4 and the exhaust port 5, and a rotating means provided inside the cylindrical path 12. 13, a liquid supply means for supplying liquid to the rotating means 13, a water supply pipe 14 as an upper supply means for supplying liquid to the upper rotating plate 16a, and a lower supplying means 18 for supplying liquid to the lower rotating plate 16b. And have.

そして、図4に示すように、回転手段13は、上下方向に向けて配置した回転軸15を有し、この回転軸15の軸方向に、回転軸15を中心として回動する複数の回転板16a、16bを所定間隔で固定している。本実施の形態では、回転軸15の上方に設けた回転板16aと、下方に設けた回転板16bとの2つを設ける構成としている。   As shown in FIG. 4, the rotating means 13 has a rotating shaft 15 arranged in the vertical direction, and a plurality of rotating plates that rotate about the rotating shaft 15 in the axial direction of the rotating shaft 15. 16a and 16b are fixed at a predetermined interval. In the present embodiment, two rotating plates 16 a provided above the rotating shaft 15 and a rotating plate 16 b provided below are provided.

そして、回転手段13の上部には、回転軸15を駆動するためのモータ17を備え、また、回転手段13の下部には、モータ17の駆動により高速回転する回転軸15および複数の回転板16a、16bを支えるための保持部(図示せず)を備えている。   A motor 17 for driving the rotating shaft 15 is provided at the upper part of the rotating means 13, and a rotating shaft 15 and a plurality of rotating plates 16 a that rotate at high speed by driving the motor 17 are provided at the lower part of the rotating means 13. , 16b is provided with a holding part (not shown).

そして、筒状の経路12の内壁には、内壁に付着した液体を下方の回転板16bへと供給する下供給手段18として、図5に示す、環状形状の貯水手段19および水路20を設けている。   An annular water storage means 19 and a water channel 20 shown in FIG. 5 are provided on the inner wall of the cylindrical path 12 as the lower supply means 18 for supplying the liquid adhering to the inner wall to the lower rotating plate 16b. Yes.

また、図4の下供給手段18は、筒状の経路12の内壁に付着した液体を下方の回転板16bへと供給するために、本実施の形態では、上方の回転板16aと下方の回転板16bとの間に、筒状の経路12の内壁に沿って図5に示す貯水手段19を設け、この貯水手段19から下方の回転板16bへと液体を供給する水路20を設ける構成とする。   Further, in the present embodiment, the lower supply means 18 in FIG. 4 supplies the liquid adhering to the inner wall of the cylindrical path 12 to the lower rotary plate 16b. A water storage means 19 shown in FIG. 5 is provided along the inner wall of the cylindrical path 12 between the plate 16b, and a water channel 20 for supplying liquid from the water storage means 19 to the lower rotating plate 16b is provided. .

複数の水路20は、図5に示すように、貯水手段19の三方から図4に示すように、筒状の経路12の中心に向かって伸びる形状で、図5に示すように、環状形状となった貯水手段19に対して等間隔に設けており、図6に示すように、各水路20から下方の回転板16bへの液体供給位置(b)は、上方の回転板16aへの液体供給位置(a)より外側としている。   As shown in FIG. 5, the plurality of water channels 20 have a shape extending from the three sides of the water storage means 19 toward the center of the cylindrical path 12 as shown in FIG. 4, and as shown in FIG. As shown in FIG. 6, the liquid supply position (b) from each water channel 20 to the lower rotary plate 16b is the liquid supply to the upper rotary plate 16a. It is outside the position (a).

そして、図4(b)および図7に示すように、液体微細化手段9と排気口5との間の液体微細化手段9側に、補助加熱手段としての補助加熱手段用の熱交換器10を設けている。   Then, as shown in FIG. 4B and FIG. 7, a heat exchanger 10 for auxiliary heating means as auxiliary heating means is provided on the side of the liquid refinement means 9 between the liquid refinement means 9 and the exhaust port 5. Is provided.

次に、液体微細化手段9を経由しない加熱用の風路(矢印B)構成を説明する。   Next, the structure of the air path for heating (arrow B) that does not pass through the liquid refinement means 9 will be described.

図3(b)の矢印Bで示すように、加熱用の風路は、ファンモータ8bからケーシング10bとダクト11bを経由し、排気チャンバー21内で、加湿用の風路(矢印A)と合流し、排気口5から排出される。   As shown by the arrow B in FIG. 3B, the heating air passage joins the humidification air passage (arrow A) in the exhaust chamber 21 from the fan motor 8b through the casing 10b and the duct 11b. And discharged from the exhaust port 5.

なお、本実施の形態では、ファンモータ8aとファンモータ8bは、2ファン1モータで構成している。   In the present embodiment, the fan motor 8a and the fan motor 8b are composed of two fans and one motor.

以上の構成において、次に動作(加湿用)を説明する。   Next, the operation (for humidification) in the above configuration will be described.

図1に示すように、サウナ室1内において、サウナを使用する場合、まず、図示していないガス湯沸かし器や電気温水器等の熱源からパイプ22を介し、図2に示すように、加熱手段用の熱交換器7および図3(b)に示す補助加熱手段用の熱交換器10に温水が供給される。   As shown in FIG. 1, when using a sauna in the sauna room 1, first, a heating means such as a gas water heater or an electric water heater (not shown) is connected to the heating means through a pipe 22 as shown in FIG. The hot water is supplied to the heat exchanger 7 and the heat exchanger 10 for auxiliary heating means shown in FIG.

この状態で、加熱手段用の熱交換器7が運転され、図3(a)、図3(b)に示すように、ファンモータ8a、ファンモータ8bが駆動されると、ファンモータ8aが吸込口4を介して図1に示すサウナ室1内の空気を吸い込み、吸い込まれた空気は加熱手段用の熱交換器7によって加熱される。   In this state, when the heat exchanger 7 for heating means is operated and the fan motor 8a and the fan motor 8b are driven as shown in FIGS. 3 (a) and 3 (b), the fan motor 8a is sucked. Air in the sauna room 1 shown in FIG. 1 is sucked through the mouth 4, and the sucked air is heated by the heat exchanger 7 for heating means.

そして、加熱された空気は、ファンモータ8aによって、ケーシング10aとダクト11aを介して、筒状の経路12の下側開口へと送られるとともに、ファンモータ8bによって、ケーシング10bとダクト11bを介して、排気チャンバー21に送られる。   The heated air is sent to the lower opening of the cylindrical path 12 by the fan motor 8a via the casing 10a and the duct 11a, and at the same time by the fan motor 8b via the casing 10b and the duct 11b. , And sent to the exhaust chamber 21.

一方、図4に示すように、モータ17が駆動されると、回転軸15が高速回転し、それにともない回転板16aおよび回転板16bが高速回転される。   On the other hand, as shown in FIG. 4, when the motor 17 is driven, the rotating shaft 15 rotates at a high speed, and accordingly, the rotating plate 16a and the rotating plate 16b are rotated at a high speed.

このとき、給水管14は、高速回転する上方の回転板16aの上面の中央近傍に水を供給する。上方の回転板16aに供給された水は、高速回転による遠心力によって外周方向に向かって薄膜状に広がり、この薄膜状になった水は、上方の回転板16aの外周縁から接線方向へと高速で吹き飛ばされる。   At this time, the water supply pipe 14 supplies water to the vicinity of the center of the upper surface of the upper rotating plate 16a that rotates at a high speed. The water supplied to the upper rotating plate 16a spreads in the form of a thin film toward the outer periphery due to the centrifugal force caused by the high-speed rotation, and this thin film-like water moves from the outer peripheral edge of the upper rotating plate 16a to the tangential direction. It is blown away at high speed.

このように、上方の回転板16aから遠心力で飛散し微細化された水の一部は、筒状の経路12の内壁に衝突して破砕され、水の微細化が加速される。   In this way, a part of the water that has been dispersed and refined by centrifugal force from the upper rotating plate 16a collides with the inner wall of the cylindrical path 12 and is crushed, and the refinement of the water is accelerated.

このように、給水管14から回転板16aの上面に供給された水は、この時点で大部分が微細化され、筒状の経路12の下側開口から流入した加熱された暖かい空気と混ざって蒸気の状態となり、筒状の経路12の上側開口から流出する。   Thus, most of the water supplied to the upper surface of the rotating plate 16a from the water supply pipe 14 is miniaturized at this time and mixed with the heated warm air flowing in from the lower opening of the cylindrical path 12. It becomes a state of steam and flows out from the upper opening of the cylindrical path 12.

一方、上方の回転板16aの回転によって筒状の経路12の内壁に衝突しても微細化されずに筒状の経路12の内壁に付着したわずかな水滴や、微細化された後に内壁において結露した微量の水滴は、筒状の経路12の内壁を伝って、図5にも示す貯水手段19に流れ落ち、貯水される。貯水手段19に貯まったわずかな水は、貯水手段19の底部に設けた傾斜により各水路20に向かって流れ、各水路20を介して、貯水手段19の三方向から、下方の回転板16bへと運ばれる。   On the other hand, even if the upper rotating plate 16a rotates and collides with the inner wall of the cylindrical path 12, a slight water droplet that does not become fine and adheres to the inner wall of the cylindrical path 12 or condensation on the inner wall after being miniaturized. The small amount of water droplets that flow along the inner wall of the cylindrical path 12 flows down to the water storage means 19 shown in FIG. A small amount of water stored in the water storage means 19 flows toward each water channel 20 by an inclination provided at the bottom of the water storage device 19, and passes through each water channel 20 from the three directions of the water storage device 19 to the lower rotating plate 16 b. It is carried.

このとき、貯水手段19に貯まったわずかな水は、貯水手段19外周の矢印で示すように、貯水手段19の底部は、水路20側に下方への傾斜すなわち貯水手段19の水路20接続部間のほぼ中央の底部を高くして、水路20接続部の底部が低くなるように傾斜を設けてあるため、貯水手段19から各水路20へ水が流れやすくなり、貯水手段19内に滞留する水を少なくでき、液体微細化手段9に残った熱によって自然に乾燥できる。   At this time, as shown by the arrow on the outer periphery of the water storage means 19, the bottom of the water storage means 19 is inclined downward toward the water channel 20, that is, between the water channel 20 connection portions of the water storage means 19 as shown in FIG. Since the slope is provided so that the bottom of the center of the water channel 20 is raised and the bottom of the water channel 20 connection portion is lowered, water can easily flow from the water storage means 19 to each water channel 20, and the water staying in the water storage means 19 And can be naturally dried by the heat remaining in the liquid refinement means 9.

また、図6に示すように、水路20から下方の回転板16bへの水供給位置bを、上方の回転板16aへの水供給位置aより外側にするのが好ましい。   Moreover, as shown in FIG. 6, it is preferable that the water supply position b from the water channel 20 to the lower rotary plate 16b is outside the water supply position a to the upper rotary plate 16a.

すなわち、水路20は水が自然に流れるように傾斜しており、この水路20を短くした構成により、上方の回転板16aと下方の回転板16bの間隔を小さくできるため、同じスペース内で回転板16aと回転板16bの枚数を増加でき、供給した水の微細化をより完全に行うことができる。   That is, the water channel 20 is inclined so that water flows naturally, and the distance between the upper rotating plate 16a and the lower rotating plate 16b can be reduced by the configuration in which the water channel 20 is shortened. The number of 16a and the rotating plate 16b can be increased, and refinement | miniaturization of the supplied water can be performed more completely.

さらに、回転板16aと回転板16bの枚数を増加することで、給水管14からの供給水量を多くしたい場合にも対応できる。   Furthermore, by increasing the number of rotating plates 16a and rotating plates 16b, it is possible to cope with a case where the amount of water supplied from the water supply pipe 14 is to be increased.

本構成は、特に浴室の天井裏など、限られたスペースに液体微細化装置を設置する場合に有効である。   This configuration is particularly effective when the liquid micronizer is installed in a limited space such as the ceiling of a bathroom.

しかし、下方の回転板16bへの温水供給位置が外側になっているため、上方の回転板16aに比べ外周縁までの距離が短く、高速回転による遠心力によって外周方向へ薄膜状に広がる面積が狭くなり、薄膜状で下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされる水量が少なくなるため、単位時間当たりの供給水量を少なくしなければならない。   However, since the hot water supply position to the lower rotating plate 16b is on the outside, the distance to the outer peripheral edge is shorter than the upper rotating plate 16a, and the area that spreads in the form of a thin film in the outer peripheral direction by centrifugal force due to high-speed rotation. The amount of water supplied per unit time must be reduced because the amount of water that is narrowed and thinly blown away at high speed from the outer peripheral edge of the lower rotating plate 16b in the tangential direction is reduced.

そのため、図5に示すように、水路20を複数設ければ、各水路20から供給する水による薄膜状の面積は狭くても、3水路合計できるため薄膜状に広がる面積を広くでき、単位時間当たりの供給水量を少なくする必要がなく、薄膜状で下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされる水量を多くできる。   Therefore, as shown in FIG. 5, if a plurality of water channels 20 are provided, even if the area of the thin film formed by the water supplied from each water channel 20 is small, the total of the three water channels can be combined, so that the area spreading in the thin film can be widened, and unit time It is not necessary to reduce the amount of water supplied per hit, and the amount of water blown off at high speed from the outer peripheral edge of the lower rotating plate 16b in the thin film shape to the tangential direction can be increased.

さらに、図6に示す複数の水路20を、環状形状となった貯水手段19に対し等間隔に設けることにより、各水路20から下方の回転板16bへ供給された水による、下方の回転板16b上での薄膜の広がりが重ならず、薄膜状で下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされる水量を多くできる。   Further, by providing a plurality of water channels 20 shown in FIG. 6 at equal intervals with respect to the water storage means 19 having an annular shape, the lower rotating plate 16b by the water supplied from each water channel 20 to the lower rotating plate 16b. The spread of the thin film does not overlap, and the amount of water blown away at high speed from the outer peripheral edge of the lower rotating plate 16b in the thin film form in the tangential direction can be increased.

また、図4に示すように、貯水手段19に貯まったわずかな水を下方の回転板16bへ流すため、水路20の底部を、貯水手段19側から回転軸15へ向かって、下方の回転板16b側へ、1〜10°傾斜させることが好ましい。この傾斜角は大きすぎると、回転板16aと回転板16bとの間隔を大きくする必要があり、設置面の水平性を考慮すると、5〜10°がより好ましい。   Also, as shown in FIG. 4, in order to allow a small amount of water stored in the water storage means 19 to flow to the lower rotating plate 16b, the bottom of the water channel 20 is moved downward from the water storing means 19 side toward the rotating shaft 15. It is preferable to incline 1 to 10 ° toward the 16b side. If this inclination angle is too large, it is necessary to increase the distance between the rotating plate 16a and the rotating plate 16b. In consideration of the horizontalness of the installation surface, 5 to 10 ° is more preferable.

また、微細化終了時において、供給した水をほぼすべて微細化するためには、上方の回転板16aより下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされる水に対し、乾燥空気を当てる、すなわち、図2の矢印Aに示すように、送風手段としてのファンモータ8aにより、筒状の経路12内を下から上へ空気を流す。   Further, at the end of the miniaturization, in order to refine the supplied water almost entirely, dry air is used against water blown at high speed from the outer peripheral edge of the rotary plate 16b below the upper rotary plate 16a to the tangential direction. That is, as shown by an arrow A in FIG. 2, air is caused to flow from the bottom to the top in the cylindrical path 12 by a fan motor 8 a as a blowing means.

そして、図3および図7に示すように、補助加熱手段としての補助加熱手段用の熱交換器10を、液体微細化手段9の上方向に開口した筒状の経路と排気口5との間に設けた構成とする。   Then, as shown in FIGS. 3 and 7, the heat exchanger 10 for the auxiliary heating means as the auxiliary heating means is disposed between the cylindrical path opened upward of the liquid refinement means 9 and the exhaust port 5. The configuration provided in

このように構成することで、微細化しきれなかった液体は、補助加熱手段としての補助加熱手段用の熱交換器10にて気化させるので、結果として、液体の微細化時に大量の排液が発生しないものとなる。   By configuring in this way, the liquid that could not be miniaturized is vaporized in the heat exchanger 10 for the auxiliary heating means as the auxiliary heating means. As a result, a large amount of drainage is generated when the liquid is miniaturized. It will not do.

また、回転板16a、16bの回転による音が、補助加熱手段としての補助加熱手段用の熱交換器10により遮られ、排気口5から回転板16a、16bの音が出ることがなくなり、結果、騒音を防止することができることにもなる。   Further, the sound due to the rotation of the rotating plates 16a and 16b is blocked by the heat exchanger 10 for the auxiliary heating means as the auxiliary heating means, and the sound of the rotating plates 16a and 16b is not emitted from the exhaust port 5, and as a result, Noise can also be prevented.

また、図5に示すように、水路20を構成する両側の側面は、それぞれ水路20外へと傾斜させることが好ましい。これにより、筒状の経路12内の下から上への空気の流れに対する抵抗を少なくでき、筒状の経路12内の圧力損失を低減できる。ここで、水路20の垂直断面はU字形状でもよく、両側の側面の傾斜は、U字の最下端を起点に両側の側面を構成しているので、両側の側面は傾斜していると言える。   Further, as shown in FIG. 5, the side surfaces on both sides constituting the water channel 20 are preferably inclined to the outside of the water channel 20. Thereby, the resistance with respect to the air flow from the bottom in the cylindrical path | route 12 can be decreased, and the pressure loss in the cylindrical path | route 12 can be reduced. Here, the vertical cross section of the water channel 20 may be U-shaped, and the slopes of the side surfaces on both sides constitute the side surfaces on both sides starting from the lowest end of the U-shape, so it can be said that the side surfaces on both sides are sloped. .

また、貯水手段19と水路20を一体で構成すれば、部品点数が少なく精度良く製造することができる。   Moreover, if the water storage means 19 and the water channel 20 are comprised integrally, it can manufacture with sufficient accuracy with few parts.

このように、上方の回転板16aに供給された温水は、上方の回転板16aが高速回転することによって大部分が微細化されるのに加え、わずかに残った微細化されなかった一部の水滴も、筒状の経路12に設けた下供給手段18を介して、高速回転する下方の回転板16bへと運ばれ、上方の回転板16aと同様に下方の回転板16bが高速回転することにより、微細化が行われる。   As described above, the hot water supplied to the upper rotating plate 16a is largely refined by the high speed rotation of the upper rotating plate 16a, and a part of the remaining non-miniaturized portion remains. Water droplets are also conveyed to the lower rotating plate 16b that rotates at a high speed via the lower supply means 18 provided in the cylindrical path 12, and the lower rotating plate 16b rotates at a high speed in the same manner as the upper rotating plate 16a. Thus, miniaturization is performed.

すなわち、筒状の経路12の内壁から、貯水手段19および水路20を介して、下方の回転板16bに供給されたわずかな水滴は、高速回転による遠心力で下方の回転板16bの外周方向に向かって薄膜状に広がって、外周縁から接線方向へと高速で吹き飛ばされ、吹き飛ばされた水滴が筒状の経路12の内壁に衝突して破砕され、水の微細化が促進されるとともに、筒状の経路12内を下から上へ流れる高温低湿の乾燥空気と混合し、ほぼ完全に微細化される。   That is, slight water droplets supplied from the inner wall of the cylindrical path 12 to the lower rotating plate 16b through the water storage means 19 and the water channel 20 are moved in the outer peripheral direction of the lower rotating plate 16b by centrifugal force due to high speed rotation. It spreads in the form of a thin film toward the tangential direction from the outer peripheral edge, blown off at high speed, and the blown water droplets collide with the inner wall of the cylindrical path 12 to be crushed, thereby promoting the miniaturization of water and It is mixed with high-temperature, low-humidity dry air flowing from the bottom to the top in the shape of the channel 12 and is almost completely refined.

一方、筒状の経路12の下側開口から液体微細化手段9へ流入した高温低湿の乾燥空気は、まず下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされた水と接触し、水を微細化して、湿度が上昇するとともに、気化熱を奪われ、温度は少し下がった空気となる。   On the other hand, the high-temperature, low-humidity dry air that has flowed into the liquid refinement means 9 from the lower opening of the cylindrical path 12 first comes into contact with the water blown away from the outer peripheral edge of the lower rotating plate 16b in a tangential direction. When water is refined, the humidity rises, the heat of vaporization is lost, and the temperature is lowered slightly.

次に、筒状の経路12内を下から上へ上昇し、上方の回転板16aの外周縁から接線方向へと高速で吹き飛ばされた水と接触し、水を微細化して、さらに湿度が上昇するとともに、さらに気化熱を奪われ、温度の低下した空気となる。   Next, the inside of the cylindrical path 12 rises from the bottom to the top, comes into contact with water blown away at high speed from the outer peripheral edge of the upper rotating plate 16a, refines the water, and further increases the humidity. At the same time, the heat of vaporization is further deprived, and the temperature is lowered.

しかし、湿度が上昇し、気化熱を奪われ温度が低下した空気は、図3(b)および図7に示すように、補助加熱手段用熱交換器により温度を上昇させるとともに、微細化されていない水を気化させ、ほぼ全て微細化させた水を含んだ空気となる。   However, the air whose humidity has been increased and the heat of vaporization has been deprived and whose temperature has been lowered has been refined while the temperature has been raised by the heat exchanger for auxiliary heating means, as shown in FIGS. Vaporize no water, and almost completely refined air.

このように、上方の回転板16aおよび下方の回転板16bの高速回転によって微細化された温水を含む高湿の空気は、図3(b)に示すように、ファンモータ8aの送風によって、筒状の経路12の上部開口から排気チャンバー21に送られ、排気チャンバー21内で、加熱用の風路(矢印B)を通ってきた高温乾燥空気と混合することにより、気化熱により低下した温度が更に上がり、排気口5からサウナ室1の内部へ供給される。   In this way, the high-humidity air containing the hot water refined by the high-speed rotation of the upper rotating plate 16a and the lower rotating plate 16b is converted into a cylinder by blowing air from the fan motor 8a as shown in FIG. The temperature lowered by the heat of vaporization is sent to the exhaust chamber 21 from the upper opening of the path 12 and mixed with the high-temperature dry air that has passed through the heating air passage (arrow B) in the exhaust chamber 21. It further rises and is supplied from the exhaust port 5 to the inside of the sauna room 1.

また、このサウナ運転を中断あるいは停止した場合には、ファンモータ8a、ファンモータ8bと回転手段13の回転板および給水管14からの給水が停止する。そのときには、給水管14からそれまでに供給された水は、上方の回転板16aおよび下方の回転板16bの高速回転によって、ほぼすべて微細化されている。   Further, when the sauna operation is interrupted or stopped, water supply from the fan motor 8a, the fan motor 8b and the rotating plate of the rotating means 13 and the water supply pipe 14 is stopped. At that time, the water supplied so far from the water supply pipe 14 is almost all made fine by the high-speed rotation of the upper rotating plate 16a and the lower rotating plate 16b.

以上のような構成と動作によれば、上述のとおり、図4に示すように、高速回転する回転手段13とこの回転手段13に液体を供給する給水管14とを備え、回転手段13において上方の回転板16a、下方の回転板16bを回転軸15方向に備える構成としたことにより、上方の回転板16aでは微細化されなかった、わずかに残った液体を、下方の回転板16bによって微細化することができるため、供給された液体を段階に分けて、ほぼ完全に微細化することが可能となるという効果を奏する。非微細化液体がわずかに残ったとしても、特別に排出せずとも液体微細化手段9に残った熱によって自然に乾燥できる程度の分量となる。   According to the above configuration and operation, as described above, as shown in FIG. 4, the rotating means 13 that rotates at high speed and the water supply pipe 14 that supplies liquid to the rotating means 13 are provided. Since the rotary plate 16a and the lower rotary plate 16b are provided in the direction of the rotary shaft 15, the slightly remaining liquid that was not refined by the upper rotary plate 16a is refined by the lower rotary plate 16b. Therefore, there is an effect that the supplied liquid can be divided into stages and can be almost completely miniaturized. Even if a small amount of the non-micronized liquid remains, the amount is such that it can be dried naturally by the heat remaining in the liquid micronizing means 9 without being specifically discharged.

また、液体供給手段としての給水管14から液体が供給される上方の回転板16a、下方の回転板16bの外周に筒状の経路12を設け、この筒状の経路12の内壁に付着した微細化されなかった液体を、下方の回転板16bへと供給する下供給手段18を設ける構成としたことにより、上方の回転板16aから飛散して筒状の経路12の内側に付着したわずかな非微細化液体を回転手段13に戻し、下方の回転板16bによってほぼ完全に微細化することが可能となるため、供給したすべての温水を効率よく微細化することが可能となるという効果を奏する。   Further, a cylindrical path 12 is provided on the outer periphery of the upper rotating plate 16a and the lower rotating plate 16b to which the liquid is supplied from the water supply pipe 14 serving as a liquid supply means, and the fine adhered to the inner wall of the cylindrical path 12 Since the lower supply means 18 for supplying the liquid that has not been converted to the lower rotating plate 16b is provided, a slight amount of non-spraying scattered from the upper rotating plate 16a and adhering to the inside of the cylindrical path 12 is obtained. Since the micronized liquid is returned to the rotating means 13 and can be almost completely refined by the lower rotating plate 16b, there is an effect that all the supplied hot water can be efficiently miniaturized.

また、図4〜図6に示す下供給手段18は、筒状の経路12の内壁に設けた貯水手段19と、この貯水手段19の三方から下方の回転板16bへと液体を供給する水路20を備えた構成としたことにより、上方の回転板16aから吹き飛ばされ、筒状の経路12の内側に付着した非微細化液体を貯水手段19に貯めて、そこに貯めた温水を、水路20を介して、高速回転する下方の回転板16bに戻すことによって、給水管14から供給した温水を確実に集めて、ほぼ完全に微細化することが可能となる。   4 to 6 includes a water storage means 19 provided on the inner wall of the cylindrical path 12, and a water channel 20 for supplying liquid from three sides of the water storage means 19 to the lower rotating plate 16b. The non-micronized liquid blown off from the upper rotating plate 16a and adhered to the inside of the cylindrical path 12 is stored in the water storage means 19, and the hot water stored therein is supplied to the water path 20 Thus, by returning to the lower rotating plate 16b that rotates at a high speed, it is possible to reliably collect hot water supplied from the water supply pipe 14 and make it almost completely fine.

また、図6に示すように、水路20から下方の回転板16bへの水供給位置を、上方の回転板16aへの水供給位置より外側にした構成により、上方の回転板16aと下方の回転板16bとの間隔を小さくできるため、同じスペース内で回転板16a、回転板16bの枚数を増加でき、供給した水の微細化をより完全に行うことができる。   Further, as shown in FIG. 6, the water supply position from the water channel 20 to the lower rotary plate 16b is set outside the water supply position to the upper rotary plate 16a, so that the upper rotary plate 16a and the lower rotation are rotated. Since the distance from the plate 16b can be reduced, the number of the rotary plates 16a and 16b can be increased in the same space, and the supplied water can be refined more completely.

また、図5に示すように、水路20を複数設けることにより、下方の回転板16b上で薄膜状に広がる面積を広くでき、薄膜状で下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされる水量を多くでき、供給した温水の微細化をより完全に行うことができる。   Further, as shown in FIG. 5, by providing a plurality of water channels 20, the area that spreads in a thin film shape on the lower rotating plate 16b can be widened, and the thin film has a high speed in the tangential direction from the outer periphery of the lower rotating plate 16b. The amount of water blown off can be increased, and the supplied hot water can be refined more completely.

さらに、複数の水路20を、環状形状となった貯水手段19に対して等間隔に設けることにより、各水路20から下方の回転板16bへ供給された水による、下方の回転板16b上での薄膜の広がりが重ならず、薄膜状で下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされる水量を多くでき、供給した温水の微細化をより完全に行うことができる。   Furthermore, by providing a plurality of water channels 20 at equal intervals with respect to the water storage means 19 having an annular shape, the water supplied from each water channel 20 to the lower rotating plate 16b on the lower rotating plate 16b. The spread of the thin films does not overlap, and the amount of water blown away at high speed from the outer peripheral edge of the lower rotating plate 16b in the thin film form can be increased, so that the supplied hot water can be refined more completely.

なお、本実施の形態では、水路20を3本設けた構成としたが、水路20から下方の回転板16bへの水供給位置が外周に近づくに従い、薄膜状に広がる面積を広くするためには、水路20を数多くしなければならない。しかし、あまり多くすると薄膜の広がりが重なり、薄膜状で下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされる水量を多くできないとともに、通風路を遮るため、水路20の数は3〜6本が好ましい。   In addition, in this Embodiment, it was set as the structure which provided the three water channels 20, However, In order to enlarge the area which spreads in a thin film shape as the water supply position from the water channel 20 to the lower rotating plate 16b approaches an outer periphery. A lot of waterways 20 must be made. However, if the number is too large, the thin film spreads, and the amount of water blown at high speed from the outer peripheral edge of the lower rotating plate 16b in the thin film shape cannot be increased at a high speed and the air passages are blocked. Six are preferable.

また、貯水手段19の底部は、水路20側に下方への傾斜を設けてあるため、各水路20へほとんどの水を流せ、貯水手段19内に滞留する水を少なくでき、液体微細化手段9に残った熱によって自然に乾燥できるという効果を奏する。   Further, since the bottom of the water storage means 19 is provided with a downward slope on the water channel 20 side, most of the water can flow through each water channel 20, and the amount of water remaining in the water storage means 19 can be reduced. It has the effect of being able to dry naturally with the heat remaining in it.

また、図3(a)、図3(b)に示すように、送風手段としてのファンモータ8aにより、筒状の経路12内を下から上へ空気を流すことにより、下方の回転板16bの外周縁から接線方向へと高速で吹き飛ばされる水に対し、より高温で乾燥した空気を当てることができるため、供給した水の微細化をより完全に行うことができる。   Further, as shown in FIGS. 3A and 3B, the fan motor 8a as the air blowing means causes air to flow from the bottom to the top in the cylindrical path 12 so that the lower rotating plate 16b Since the air dried at a higher temperature can be applied to the water blown away at high speed from the outer peripheral edge to the tangential direction, the supplied water can be refined more completely.

また、水路20を構成する両側の側面を、それぞれ水路20外へと傾斜させた構成とすることにより、筒状の経路12内の下から上への空気の流れに対する抵抗を少なくでき、筒状の経路12内の圧力損失を低減できるという効果を奏する。   In addition, by making the side surfaces on both sides constituting the water channel 20 be inclined to the outside of the water channel 20, resistance to the air flow from the bottom to the top in the cylindrical channel 12 can be reduced, and the cylindrical shape The pressure loss in the path 12 can be reduced.

また、本体ケース6内の吸込口4と排気口5を結ぶ風路を分岐させ、一方の風路にのみ液体微細化手段9を設けた構成とすることにより、液体微細化手段9を経由する加湿用の風路からの空気と、液体微細化手段9を経由しない加熱用の風路からの空気を排気チャンバー21内で混合でき、適度な温湿度の空気を排気口5からサウナ室1の内部へ供給することができるという効果を奏する。   Further, the air passage connecting the suction port 4 and the exhaust port 5 in the main body case 6 is branched, and the liquid refinement means 9 is provided only in one of the air passages, thereby passing through the liquid refinement means 9. The air from the air passage for humidification and the air from the air passage for heating not passing through the liquid refining means 9 can be mixed in the exhaust chamber 21, and air of appropriate temperature and humidity can be mixed into the sauna room 1 from the exhaust port 5. There is an effect that it can be supplied to the inside.

また、水路20の底部を、貯水手段19側から回転軸15へ向かって、下方の回転板16b側へ、1〜10°傾斜させることにより、貯水手段19に貯まったわずかな水を下方の回転板16bへ自然に流すことができる。   Further, by tilting the bottom portion of the water channel 20 by 1 to 10 degrees from the water storage means 19 side toward the rotation shaft 15 toward the lower rotating plate 16b side, a slight amount of water stored in the water storage means 19 is rotated downward. It can flow naturally to the plate 16b.

また、貯水手段19と水路20を一体で構成すれば、部品点数が少なく精度良く製造することができる。   Moreover, if the water storage means 19 and the water channel 20 are comprised integrally, it can manufacture with sufficient accuracy with few parts.

なお、図4と図6に示す突起23は、水が筒状の経路12の内壁に衝突する際に、微細化を促進するために設けられている。   The projections 23 shown in FIGS. 4 and 6 are provided to promote miniaturization when water collides with the inner wall of the cylindrical path 12.

なお、複数の回転板16a、16bの回転数は、3000rpm(rpmは毎分の回転数を表す単位)より低い回転数とすることにより、高速回転による騒音を抑えることが可能となるという効果を奏する。   The rotational speed of the plurality of rotating plates 16a and 16b is set to a rotational speed lower than 3000 rpm (rpm is a unit representing the rotational speed per minute), thereby making it possible to suppress noise due to high-speed rotation. Play.

なお、給水管14から供給する水は温水でもよく、給水管14から60g/分以下で供給する構成とすると、供給した水あるいは温水を、上方の回転板16aおよび下方の回転板16bによって3000rpmの回転数において、ほぼ完全に微細化することが可能となるという効果を奏する。   The water supplied from the water supply pipe 14 may be hot water. If the water supply pipe 14 is supplied at a rate of 60 g / min or less, the supplied water or hot water is supplied at 3000 rpm by the upper rotary plate 16a and the lower rotary plate 16b. There is an effect that the rotation speed can be almost completely miniaturized.

このように、上記の液体微細化装置3をサウナ室1に設置してサウナ装置として利用した場合、供給した液体をほぼ完全に微細化することができ、わずかに残った非微細化液体を特別に排出せずとも、液体微細化手段9に残った熱によって自然に乾燥できる程度の分量となるので、微細化できなかった温水を排水として処理するための配管施工の工事が不要となり、結果として、サウナ装置の施工作業が簡単になるという効果を奏する。   As described above, when the liquid refining device 3 is installed in the sauna chamber 1 and used as a sauna device, the supplied liquid can be almost completely refined, and the remaining non-micronized liquid is specially selected. Even if it is not discharged, the amount of water that can be naturally dried by the heat remaining in the liquid micronization means 9 is sufficient, so that piping work for treating the hot water that could not be micronized as wastewater becomes unnecessary. There is an effect that the construction work of the sauna device is simplified.

しかも、液体供給手段は、上方の回転板に液体を供給する上供給手段と、下方の回転板に液体を供給する下供給手段とを有し、この下供給手段は、前記筒状の経路の内壁に設けた貯水手段と、この貯水手段から下方の回転板へ液体を供給する水路とを有し、この水路から下方の回転板への液体供給位置は、上方の回転板への液体供給位置より外側である構成とすることにより、水路が短くなるため、回転板の間隔を小さくでき、回転板の数量を増やしても液体微細化装置の小型化が実現できる。   In addition, the liquid supply means has an upper supply means for supplying liquid to the upper rotating plate and a lower supply means for supplying liquid to the lower rotating plate, and the lower supply means has the cylindrical path. A water storage means provided on the inner wall and a water channel for supplying liquid from the water storage means to the lower rotating plate, the liquid supply position from the water path to the lower rotating plate is the liquid supply position to the upper rotating plate. Since the water channel is shortened by adopting an outer configuration, the interval between the rotating plates can be reduced, and the liquid miniaturization apparatus can be downsized even if the number of rotating plates is increased.

以上のように、本発明の液体微細化装置は、液体を効率よく、ほぼ完全に微細化することが可能となるため、微細化されなかった液体を特別に排出しなくても自然に乾燥させることもできるので、排液手段を別途設ける必要のないものとなる。   As described above, the liquid miniaturization apparatus of the present invention enables efficient and almost complete micronization of the liquid. Therefore, the liquid that has not been miniaturized can be naturally dried without special discharge. Therefore, it is not necessary to provide a drainage means separately.

したがって、例えば、サウナ装置、加湿装置、冷却装置、噴霧装置、洗浄装置、植物育成設備等への活用が期待される。また、温水だけでなく、油や洗剤等のその他の液体の微細化設備にも利用することが可能である。   Therefore, for example, utilization to a sauna device, a humidifier, a cooling device, a spraying device, a cleaning device, a plant growing facility, and the like is expected. Moreover, it can be used not only for warm water but also for other liquid refining equipment such as oil and detergent.

4 吸込口
5 排気口
6 本体ケース
7 熱交換器
8a、8b ファンモータ
9 液体微細化手段
10 熱交換器
10a、10b ケーシング
11a、11b ダクト
12 筒状の経路
13 回転手段
14 給水管
15 回転軸
16a、16b 回転板
17 モータ
18 下供給手段
19 貯水手段
20 水路
21 排気チャンバー
22 パイプ
23 突起
DESCRIPTION OF SYMBOLS 4 Suction port 5 Exhaust port 6 Main body case 7 Heat exchanger 8a, 8b Fan motor 9 Liquid refinement means 10 Heat exchanger 10a, 10b Casing 11a, 11b Duct 12 Cylindrical path 13 Rotating means 14 Water supply pipe 15 Rotating shaft 16a 16b Rotating plate 17 Motor 18 Lower supply means 19 Water storage means 20 Water passage 21 Exhaust chamber 22 Pipe 23 Projection

Claims (12)

吸込口と排気口を有する本体ケースと、この本体ケース内の前記吸込口と前記排気口を結ぶ風路に設けた加熱手段および送風手段と、この送風手段と前記排気口間の風路内に設けた液体微細化手段とを備え、前記液体微細化手段は、上下方向に開口した筒状の経路と、この筒状の経路内に設けた回転手段と、この回転手段に液体を供給する液体供給手段とを有し、前記回転手段は、上下方向に向けて配置した回転軸と、この回転軸の軸方向に所定間隔で固定した複数の回転板とを有し、前記液体供給手段は、上方の回転板に液体を供給する上供給手段と、下方の回転板に液体を供給する下供給手段とを有し、この下供給手段は、前記筒状の経路の内壁に設けた貯水手段と、この貯水手段から下方の回転板へ液体を供給する水路とを有し、この水路から下方の回転板への液体供給位置は、上方の回転板への液体供給位置より外側に配置し、補助加熱手段を前記液体微細化手段と前記排気口との間に設けたことを特徴とする液体微細化装置。 A main body case having a suction port and an exhaust port, a heating unit and a blower unit provided in an air passage connecting the suction port and the exhaust port in the main body case, and an air path between the blower unit and the exhaust port Liquid refinement means provided, and the liquid refinement means includes a cylindrical path that opens in the vertical direction, a rotation means provided in the cylindrical path, and a liquid that supplies liquid to the rotation means. Supply means, the rotation means has a rotation shaft arranged in the vertical direction, and a plurality of rotation plates fixed at predetermined intervals in the axial direction of the rotation shaft, the liquid supply means, An upper supply means for supplying liquid to the upper rotating plate; and a lower supply means for supplying liquid to the lower rotating plate, the lower supply means comprising: water storage means provided on the inner wall of the cylindrical path; And a water channel for supplying liquid from the water storage means to the lower rotating plate. The liquid supply position from the path to the lower rotary plate is arranged outside the liquid supply position to the upper rotary plate, and auxiliary heating means is provided between the liquid miniaturizing means and the exhaust port. Liquid refinement device. 補助加熱手段を、液体微細化手段の上方向に開口した筒状の経路と排気口との間に設けたことを特徴とする請求項1に記載の液体微細化装置。 2. The liquid refinement apparatus according to claim 1, wherein the auxiliary heating means is provided between a cylindrical path opened upward of the liquid refinement means and the exhaust port. 加熱手段および補助加熱手段を、温水による加熱とすることを特徴とする請求項1または2記載の液体微細化装置。 The liquid refinement apparatus according to claim 1 or 2, wherein the heating means and the auxiliary heating means are heated by warm water. 水路を、複数設けたことを特徴とする請求項1に記載の液体微細化装置。 The liquid refinement apparatus according to claim 1, wherein a plurality of water channels are provided. 水路は、環状形状となった貯水手段に対し、等間隔に設けたことを特徴とする請求項4に記載の液体微細化装置。 The liquid refinement apparatus according to claim 4, wherein the water channel is provided at equal intervals with respect to the water storage means having an annular shape. 送風手段により、筒状の経路内を下から上へ空気を流すことを特徴とする請求項1に記載の液体微細化装置。 The liquid refinement apparatus according to claim 1, wherein air is caused to flow in the cylindrical path from the bottom to the top by the blowing means. 水路を構成する両側の側面は、その上端がそれぞれ水路外へと傾斜させたことを特徴とする請求項6に記載の液体微細化装置。 The liquid micronizer according to claim 6, wherein the side surfaces of both sides constituting the water channel have their upper ends inclined to the outside of the water channel. 本体ケース内の吸込口と排気口を結ぶ風路を分岐させ、一方の風路にのみ液体微細化手段を設けたことを特徴とする請求項1に記載の液体微細化装置。 2. The liquid refinement apparatus according to claim 1, wherein the air passage connecting the suction port and the exhaust port in the main body case is branched, and the liquid refinement means is provided only in one of the air passages. 貯水手段の底部は、水路側に下方への傾斜を設けたことを特徴とする請求項1に記載の液体微細化装置。 The liquid refining apparatus according to claim 1, wherein the bottom of the water storage means is provided with a downward slope on the water channel side. 水路の底部は、貯水手段側から回転軸へ向かって下方の回転板側へ1〜10°傾斜させたことを特徴とする請求項1に記載の液体微細化装置。 2. The liquid micronizer according to claim 1, wherein the bottom of the water channel is inclined by 1 to 10 [deg.] From the water storage means side toward the rotating shaft toward the rotating shaft. 貯水手段と水路を、一体で構成としたことを特徴とする請求項1に記載の液体微細化装置。 The liquid refining device according to claim 1, wherein the water storage means and the water channel are integrally configured. 請求項1〜11のいずれか一つに記載の液体微細化装置をサウナ室に設置したサウナ装置。 The sauna apparatus which installed the liquid refinement | purification apparatus as described in any one of Claims 1-11 in the sauna room.
JP2009167413A 2008-09-09 2009-07-16 Liquid refinement device and sauna device using the same Expired - Fee Related JP5287567B2 (en)

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PCT/JP2009/004430 WO2010029722A1 (en) 2008-09-09 2009-09-08 Liquid refining device and humidifier using same
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