JP2006181290A - Bathtub apparatus - Google Patents

Bathtub apparatus Download PDF

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JP2006181290A
JP2006181290A JP2004381387A JP2004381387A JP2006181290A JP 2006181290 A JP2006181290 A JP 2006181290A JP 2004381387 A JP2004381387 A JP 2004381387A JP 2004381387 A JP2004381387 A JP 2004381387A JP 2006181290 A JP2006181290 A JP 2006181290A
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oxygen
enriched air
bath water
bathtub
amount
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Noriyuki Kitachi
範行 北地
Shigeyuki Yamaguchi
重行 山口
Kazumasa Rokushima
一雅 六嶋
Yasunari Maeda
康成 前田
Hisanori Shibata
尚紀 柴田
Yoshiyasu Ito
良泰 伊藤
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Panasonic Electric Works Co Ltd
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Matsushita Electric Works Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a bathtub apparatus capable of extending a time required for lowering a moisture content of the keratin after taking a bath, providing a person after taking the bath with an enough time for leisurely caring the skin with face lotion with the skin state moisturized, improving the moisturizing effect and improving the skin into moisturized one. <P>SOLUTION: This bathtub apparatus is provided with an oxygen enriched air supply means 2 supplying oxygen enriched air including oxygen with higher concentration than the oxygen concentration in air into bathwater W in a bathtub 1. The amount of dissolved oxygen in the bathwater is retained to 7-13 ml/L by the oxygen enriched air supply means 2 supplying the oxygen enriched air into the bathwater in the bathtub 1. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、浴槽内の浴水中における溶存酸素量を通常よりも多くする浴槽装置に関するものである。   The present invention relates to a bathtub device that increases the amount of dissolved oxygen in bath water in a bathtub.

湯上り後の肌が湿った状態で化粧水などにより肌の手入れをすると保湿効果を高め、モイスチャー効果により肌がしっとりすると言われている。   It is said that if the skin is moistened with a lotion or the like after the bath has been moistened, the moisturizing effect is enhanced, and the moisturizing effect moisturizes the skin.

しかしながら、入浴すると一時的に人の皮膚の角質の水分量が増えて肌が湿った状態になるが、入浴することにより、皮膚の表面を覆っていた皮脂が剥がれるので、湯上り後短時間(約10分〜13分程度)で角質の水分量が急激に低下して入浴前よりも乾燥した肌となってしまう。このため、通常の入浴においては、湯上り後、短時間のうちに化粧水などによる肌の手入れをしないと、上記保湿効果を高めることができない。   However, when bathing, the amount of moisture in the skin of a person's skin temporarily increases and the skin becomes moist, but when bathing, the sebum covering the surface of the skin is peeled off, so a short time (about approx. In about 10 to 13 minutes), the amount of water in the keratin is drastically reduced, resulting in a dry skin than before bathing. For this reason, in normal bathing, the above moisturizing effect cannot be enhanced unless the skin is cleaned with a lotion or the like within a short time after bathing.

ところが、湯上り後には身体を拭いたり、衣服を着たりするための時間が必要であり、湯上り後、約10分〜13分という短時間のうちに化粧水などによる肌の手入れをするのは、きわめて煩わしく、また、上記の短時間では肌の手入れするのに十分な時間ではない。このため、湯上り後、約10分〜13分という短時間のうちに化粧水などによる肌の手入れをする人は少なく、湯上り後、ある程度時間が経過した後に化粧水などによる肌の手入れをする人が多く、効果的に保湿効果を高めることができないという問題があった。   However, after bathing, it takes time to wipe the body and wear clothes. After bathing, cleaning the skin with lotion within a short time of about 10 to 13 minutes It is extremely troublesome, and the above-mentioned short time is not sufficient time for skin care. For this reason, there are few people who care for skin with lotion within a short time of about 10 to 13 minutes after bathing, and people who care for skin with lotion after some time has passed after bathing. There is a problem that the moisturizing effect cannot be effectively enhanced.

また、近年、浴槽に微細気泡発生装置を設け、浴槽内から吸い込んだ浴水に空気を溶解させると共に空気を溶解した浴水を浴槽内に吐出して浴槽内で微細気泡を発生するようにした微細気泡発生浴槽装置が提供されている(例えば、特許文献1参照)。   In recent years, a microbubble generator has been installed in the bathtub to dissolve the air in the bath water sucked from the bathtub and to discharge the bath water in which the air is dissolved into the bathtub to generate microbubbles in the bathtub. A microbubble generating bathtub device is provided (see, for example, Patent Document 1).

この特許文献1に示された従来例にあっては、空気が微細気泡となって浴水中に供給されるが、単に大気中の空気(酸素濃度21%)を浴水に溶解させて微細気泡を発生するだけのため、浴水中における溶存酸素量は微細気泡を発生させない場合と殆ど変わらず、また、微細気泡の発生を長時間続けても浴水中の溶存酸素量は殆ど変化しない。   In the conventional example shown in Patent Document 1, air is supplied as fine bubbles into the bath water. However, air in the atmosphere (oxygen concentration 21%) is simply dissolved in the bath water to form fine bubbles. Therefore, the amount of dissolved oxygen in the bath water is almost the same as when fine bubbles are not generated, and the amount of dissolved oxygen in the bath water hardly changes even if the generation of fine bubbles is continued for a long time.

ところで、浴水中の溶存酸素量が少ないと浴水の酸素分圧が低く、浸透圧により浴水中の酸素が角質内に供給されにくい。このため、浴水中の溶存酸素が角質内天然保湿因子(NMF)に作用せず、水分保持能力を向上させることがない。   By the way, if the amount of dissolved oxygen in the bath water is small, the oxygen partial pressure of the bath water is low, and the oxygen in the bath water is difficult to be supplied into the stratum corneum due to the osmotic pressure. For this reason, the dissolved oxygen in the bath water does not act on the keratin natural moisturizing factor (NMF), and the water retention capacity is not improved.

したがって、単に大気中の空気(酸素濃度21%)を浴水に溶解させて微細気泡を発生させるようにした浴槽装置においても湯上り後短時間(約10分〜13分程度)で角質の水分量が急激に低下して乾燥した肌となってしまって、前述の普通の浴槽装置と同様の問題がある。また、単に大気中の空気(酸素濃度21%)を浴水に溶解させて微細気泡を発生するだけのためにさほど快適度が向上せず、また心肺機能の負担軽減にならない。
特開2002−330885号公報
Therefore, even in a bathtub apparatus in which air in the atmosphere (oxygen concentration 21%) is simply dissolved in bath water to generate fine bubbles, the amount of horny water in a short time (about 10 to 13 minutes) after bathing Drops rapidly and becomes dry skin, and there is a problem similar to the above-mentioned ordinary bathtub apparatus. In addition, since air in the atmosphere (oxygen concentration 21%) is simply dissolved in the bath water to generate fine bubbles, the comfort level is not improved so much and the burden on the cardiopulmonary function is not reduced.
JP 2002-330885 A

本発明は上記の従来の問題点に鑑みて発明したものであって、湯上り後における角質の水分量の低下に要する時間を従来より長く延ばすことができて、湯上り後に肌が湿った状態で化粧水などにより肌の手入れを余裕を持って行うことができ、保湿効果を高めて肌をしっとりさせ、化粧ののりを良くすることができ、また、入浴中に皮膚呼吸して入浴中の快適度を上げたり心肺機能の負担軽減を図ったりできる浴槽装置を提供することを課題とするものである。   The present invention has been invented in view of the above-mentioned conventional problems, and it is possible to extend the time required for reducing the amount of water in the keratin after bathing for a longer time than before, so that makeup can be applied with the skin moist after bathing. You can take care of your skin with plenty of water, improve the moisturizing effect, moisturize your skin, improve makeup, and comfort while taking a breath while taking a bath. It is an object of the present invention to provide a bathtub device that can raise the load and reduce the burden on the cardiopulmonary function.

上記課題を解決するために本発明の浴槽装置は、空気中の酸素濃度よりも高濃度の酸素を含む酸素富化空気を浴槽1内の浴水W中に供給する酸素富化空気供給手段2を設け、該酸素富化空気供給手段2による酸素富化空気の浴槽1内の浴水中への供給により浴水中の溶存酸素量を7ml/L〜13ml/Lとすることを特徴とするものである。   In order to solve the above problems, the bathtub apparatus of the present invention is an oxygen-enriched air supply means 2 for supplying oxygen-enriched air containing oxygen at a higher concentration than the oxygen concentration in the air into the bath water W in the bathtub 1. And the amount of dissolved oxygen in the bath water is set to 7 ml / L to 13 ml / L by supplying the oxygen-enriched air into the bath water in the bathtub 1 by the oxygen-enriched air supply means 2. is there.

このような構成とすることで、通常の浴槽1内の浴水Wに比べて浴槽1内の浴水W中の溶存酸素濃度が高くなり、人の皮膚の角質の酸素分圧より浴水Wの酸素分圧が高くなり、身体の浴水W中の部位において浸透圧が生じて水分浸透が促進され、また高濃度の溶存酸素が角質内天然保湿因子(NMF)に作用し、水分保持能力を向上させる。また高濃度の溶存酸素が角質内の細胞間脂質に作用し、水分保持能力を向上させる。これらにより湯上り後における角質の水分量の低下に要する時間を長く延ばすことができて、湯上り後に肌が湿った状態で化粧水などにより肌の手入れを余裕を持って行うことができ、保湿効果を高めて肌をしっとりさせ、化粧ののりを良くすることができる。また、入浴中に皮膚呼吸ができるようになって入浴の快適度を上げると共に心肺機能の負担を軽減できる。   By adopting such a configuration, the dissolved oxygen concentration in the bath water W in the bathtub 1 becomes higher than the bath water W in the normal bathtub 1, and the bath water W is higher than the oxygen partial pressure of the horny skin of human skin. Oxygen partial pressure of the body increases, osmotic pressure is generated in the body bath water W to promote water permeation, and high concentration of dissolved oxygen acts on natural moisturizing factor (NMF) in the stratum corneum. To improve. In addition, a high concentration of dissolved oxygen acts on intercellular lipids in the stratum corneum, improving the water retention capacity. This makes it possible to prolong the time required to reduce the amount of horny water after bathing, so that the skin can be moisturized with lotion, etc. while the skin is moistened after bathing, providing a moisturizing effect. Increases and moisturizes the skin, improving the makeup paste. In addition, skin breathing can be performed during bathing, so that the comfort of bathing can be increased and the burden of cardiopulmonary function can be reduced.

また、前記酸素富化空気供給手段2からの酸素富化空気の供給を受けて浴水に酸素富化空気からなる微細気泡を発生する微細気泡発生装置3を備えることが好ましい。   Moreover, it is preferable to provide the fine bubble generator 3 which receives the supply of oxygen-enriched air from the oxygen-enriched air supply means 2 and generates fine bubbles made of oxygen-enriched air in the bath water.

このように、酸素富化空気を浴槽1の浴水W中に微細気泡として供給することで、酸素富化空気の微細気泡が浴槽1内の浴水W中に広く分散するとともに長く滞留することとなり、浴槽1内の浴水W中の溶存酸素量がまんべんなく多くなり、簡単に浴水Wの溶存酸素量を目的とする高濃度の溶存酸素量にすることができる。更に、身体の浴槽1内の浴水W中の部位がまんべんなく微細気泡により包まれた状態となり、微細気泡がお湯のぬくもりをやさしく伝え、身体の芯まで暖まり、湯冷めし難くなる。   Thus, by supplying oxygen-enriched air as fine bubbles in the bath water W of the bathtub 1, the fine bubbles of oxygen-enriched air are widely dispersed in the bath water W in the bathtub 1 and stay for a long time. Thus, the amount of dissolved oxygen in the bath water W in the bathtub 1 increases evenly, and the amount of dissolved oxygen in the bath water W can be easily set to a high concentration of dissolved oxygen. Furthermore, the part in the bath water W in the bathtub 1 of the body is evenly wrapped with fine bubbles, and the fine bubbles gently convey the warmth of hot water, warming up to the core of the body, and making it difficult to cool down.

また、酸素富化空気供給手段2から供給される酸素富化空気の酸素濃度が25%〜40%であることが好ましい。   Moreover, it is preferable that the oxygen concentration of the oxygen-enriched air supplied from the oxygen-enriched air supply means 2 is 25% to 40%.

すなわち、酸素富化空気供給手段2から供給される酸素富化空気の酸素濃度が25%に満たないと、これを浴水Wに供給しても通常の一般の浴槽1内の浴水Wの溶存酸素量と殆どかわらず、目的とする溶存酸素量にすることができない。また、酸素富化空気供給手段2から供給される酸素富化空気の酸素濃度が40%を超えると、浴水Wに溶けきらずに水面から浴室6空間内に放出される酸素富化空気の量が多くなり過ぎてしまい、浴室6空間内の酸素濃度が必要以上に高くなって身体に対する負担が大きくて好ましくない。これに対し上記のように酸素富化空気供給手段2から供給される酸素富化空気の酸素濃度が25%〜40%とすることで、浴槽1内の浴水W中の溶存酸素量を目的とする溶存酸素量できると共に浴室6内の酸素濃度が必要以上に高くならないようにできる。   That is, when the oxygen concentration of the oxygen-enriched air supplied from the oxygen-enriched air supply means 2 is less than 25%, the bath water W in the ordinary general bath 1 is supplied to the bath water W. The target amount of dissolved oxygen cannot be achieved regardless of the amount of dissolved oxygen. In addition, when the oxygen concentration of the oxygen-enriched air supplied from the oxygen-enriched air supply means 2 exceeds 40%, the amount of oxygen-enriched air released from the water surface into the bathroom 6 space without being dissolved in the bath water W. This is not preferable because the oxygen concentration in the bathroom 6 space becomes higher than necessary and the burden on the body is large. On the other hand, the oxygen concentration of the oxygen-enriched air supplied from the oxygen-enriched air supply means 2 is 25% to 40% as described above, so that the amount of dissolved oxygen in the bath water W in the bath 1 is the purpose. And the oxygen concentration in the bathroom 6 can be prevented from becoming higher than necessary.

本発明は上記のように、湯上り後における角質の水分量の低下に要する時間を長く延ばすことができて、湯上り後に肌が湿った状態で化粧水などにより肌の手入れを余裕を持って行うことができ、保湿効果を高めて肌をしっとりさせ、化粧ののりを良くすることができるという効果があり、また、入浴中に皮膚呼吸して入浴中の快適度を上げたり心肺機能の負担軽減を図ることができるという効果がある。   As described above, the present invention can prolong the time required for the decrease in the amount of horny water after bathing, and perform skin care with a lotion or the like while the skin is moistened after bathing. It has the effect of improving the moisturizing effect and moisturizing the skin, improving the makeup paste, and also increasing the comfort level during bathing and reducing the burden of cardiopulmonary function during bathing. There is an effect that it can be planned.

以下、本発明を添付図面に示す実施形態に基いて説明する。   Hereinafter, the present invention will be described based on embodiments shown in the accompanying drawings.

浴槽1内の浴水W中に空気中の酸素濃度よりも高濃度の酸素を含む酸素富化空気を浴槽1内の浴水W中に供給する酸素富化空気供給手段2を設けてある。酸素富化空気供給手段2としては、例えば、酸素富化装置2aや酸素ボンベ等を挙げることができる。以下の説明では酸素富化空気供給手段2として酸素富化装置2aを用いた例で説明する。   An oxygen-enriched air supply means 2 is provided in the bath water W in the bathtub 1 for supplying oxygen-enriched air containing oxygen at a higher concentration than the oxygen concentration in the air into the bath water W in the bathtub 1. Examples of the oxygen-enriched air supply means 2 include an oxygen enricher 2a and an oxygen cylinder. In the following description, an example in which the oxygen enrichment device 2a is used as the oxygen enriched air supply means 2 will be described.

また、以下の実施形態では、酸素富化装置2aから供給された酸素富化空気を微細気泡発生装置3により酸素富化空気からなる微細気泡として浴水W中に供給するようにしている。   In the following embodiment, oxygen-enriched air supplied from the oxygen enricher 2a is supplied into the bath water W as microbubbles made of oxygen-enriched air by the microbubble generator 3.

そして、本発明においては、酸素富化装置2aから浴槽1内の浴水Wに酸素富化空気を供給することで、浴槽1内の浴水W中の溶存酸素量を7ml/L〜13ml/Lとするようになっている。   In the present invention, oxygen-enriched air is supplied from the oxygen enricher 2a to the bath water W in the bathtub 1 to reduce the amount of dissolved oxygen in the bath water W in the bathtub 1 to 7 ml / L to 13 ml / L is set.

図1に示すように、ユニットバスルームからなる浴室6内の底部には防水床パン5を設けてあり、防水床パン5には浴槽1を設置してある。この浴槽1には浴槽1内から吸い込んだ浴水Wに空気を溶解させると共に空気を溶解させた浴水Wを浴槽1内に吐出することで微細気泡を発生する微細気泡発生装置3を設けてある。   As shown in FIG. 1, a waterproof floor pan 5 is provided at the bottom of a bathroom 6 composed of a unit bathroom, and a bathtub 1 is installed on the waterproof floor pan 5. The bathtub 1 is provided with a microbubble generator 3 that generates microbubbles by dissolving the air in the bath water W sucked from the bathtub 1 and discharging the bath water W in which the air is dissolved into the bathtub 1. is there.

微細気泡発生装置3は、図2に示すように、吸入口7と吐出口23と循環管路8とエジェクター10と循環ポンプ11と溶解タンク12とで主体が構成されている。吸入口7は浴槽1の底部に装着してあり、浴槽1内の浴水Wを吸入するようになっている。吐出口23は浴槽1の底部に装着してあり、吐出口23から浴槽1内に微細気泡を含んだ浴水Wを吐出するようになっている。この吸入口7と吐出口23とは浴槽1外に配管した循環管路8にて連通させてあり、循環管路8の途中には循環ポンプ11を配置してあり、循環ポンプ11を駆動することにより浴水Wを吸入口7から吸入して吐出口23から吐出させるようになっている。また循環管路8には吸入口7と循環ポンプ11との間に位置するようにエジェクター10を設けてあり、循環ポンプ11の駆動により浴水Wがエジェクター10を通るとき空気を吸入して浴水Wに空気を混入するようになっている。循環ポンプ11と吐出口23との間で循環管路8には溶解タンク12を配置してあり、エジェクター10で混入した空気を浴水Wに溶解させるようになっている。この溶解タンク12内では蛇行した経路に浴水Wを通過させるなどして浴水Wに空気を溶解させるようになっている。吐出口23は空気が溶解した浴水Wを減圧して吐出させることで溶解した空気が微細気泡となり、微細気泡を含んだ浴水Wを吐出させるようになっており、浴水Wが所謂ミルキー状になって入浴することができるようになっている。   As shown in FIG. 2, the fine bubble generating device 3 mainly includes a suction port 7, a discharge port 23, a circulation pipe 8, an ejector 10, a circulation pump 11, and a dissolution tank 12. The suction port 7 is attached to the bottom of the bathtub 1 and sucks the bath water W in the bathtub 1. The discharge port 23 is attached to the bottom of the bathtub 1, and the bath water W containing fine bubbles is discharged from the discharge port 23 into the bathtub 1. The suction port 7 and the discharge port 23 communicate with each other through a circulation line 8 piped outside the bathtub 1, and a circulation pump 11 is disposed in the middle of the circulation line 8 to drive the circulation pump 11. Accordingly, the bath water W is sucked from the suction port 7 and discharged from the discharge port 23. In addition, an ejector 10 is provided in the circulation line 8 so as to be positioned between the suction port 7 and the circulation pump 11, and when the bath water W passes through the ejector 10 by driving of the circulation pump 11, air is sucked into the bath. Air is mixed into the water W. A dissolution tank 12 is disposed in the circulation line 8 between the circulation pump 11 and the discharge port 23, and the air mixed in the ejector 10 is dissolved in the bath water W. In the dissolution tank 12, air is dissolved in the bath water W by passing the bath water W through a meandering path. The discharge port 23 decompresses and discharges the bath water W in which the air is dissolved, whereby the dissolved air becomes fine bubbles, and the bath water W containing fine bubbles is discharged. You can take a bath in the shape.

また浴室6の天井の上に酸素富化空気供給手段2である酸素富化装置2aを設置してある。この酸素富化装置2aは酸素富化膜と真空ポンプとで主体が構成されており、真空ポンプで大気中の空気を取り入れて有機高分子の平膜のような酸素富化膜に空気を通すことで酸素が富化された空気を得ることができるようになっている。空気を酸素富化膜に通すとき、酸素と窒素とは減速するが、酸素は窒素の約2.5倍の速度で通過する。これにより通常の大気中の空気は窒素が78%、酸素が21%であったのが、酸素富化膜によって窒素が69%、酸素が30%の空気となり、酸素富化空気が得られる。   Further, an oxygen enrichment device 2a which is oxygen enriched air supply means 2 is installed on the ceiling of the bathroom 6. This oxygen enrichment apparatus 2a is mainly composed of an oxygen enrichment film and a vacuum pump. Air in the atmosphere is taken in by the vacuum pump and air is passed through an oxygen enrichment film such as a flat film of an organic polymer. As a result, air enriched with oxygen can be obtained. When passing air through the oxygen-enriched membrane, oxygen and nitrogen decelerate, but oxygen passes at a rate approximately 2.5 times that of nitrogen. As a result, the air in the normal atmosphere was 78% nitrogen and 21% oxygen, but the oxygen-enriched film turns the air 69% nitrogen and 30% oxygen, thereby obtaining oxygen-enriched air.

この酸素富化装置2aで得られた酸素富化空気は空気供給経路4にて微細気泡発生装置3のエジェクター10に供給されるようになっている。   The oxygen-enriched air obtained by the oxygen enricher 2a is supplied to the ejector 10 of the fine bubble generator 3 through the air supply path 4.

また浴室6の天井上には制御部19を設けてある。また浴槽1のフランジ18には微細気泡発生装置3を操作する操作スイッチ20を設けてある。   A control unit 19 is provided on the ceiling of the bathroom 6. The flange 18 of the bathtub 1 is provided with an operation switch 20 for operating the fine bubble generating device 3.

しかして、酸素富化装置2aを駆動して微細気泡発生装置3の循環ポンプ11を駆動すると、図2に示すように吸入口7から浴槽1内の浴水Wが吸い込まれ、この浴水Wがエジェクター10を通過することで酸素富化空気が浴水Wに混入され、この酸素富化空気が混入された浴水Wが溶解タンク12に送られることで浴水Wに酸素富化空気が溶解し、酸素富化空気が溶解した浴水Wが吐出口23から減圧して吐出させられることにより、高酸素濃度の微細気泡を含んだ浴水Wがミルキー状に吐出される。   Then, when the oxygen enricher 2a is driven to drive the circulation pump 11 of the fine bubble generator 3, the bath water W in the bathtub 1 is sucked from the suction port 7 as shown in FIG. Passes through the ejector 10, oxygen-enriched air is mixed into the bath water W, and the bath water W mixed with this oxygen-enriched air is sent to the dissolution tank 12 so that the oxygen-enriched air is contained in the bath water W. The bath water W dissolved and dissolved in the oxygen-enriched air is discharged under reduced pressure from the discharge port 23, so that the bath water W containing fine bubbles having a high oxygen concentration is discharged in a milky manner.

上記のように酸素富化装置2aで発生した酸素富化空気を微細気泡発生装置3のエジェクター10に供給することで酸素富化空気の微細気泡を発生することができるが、この微細気泡の気泡径は200nm〜100μmとすることが望ましい。ところで、微細気泡の気泡径と気泡の上昇速度の関係を示したのが図9のグラフである。このグラフは横軸が気泡径(μm)で縦軸が上昇速度(m/s)であり、気泡径が小さい程気泡の上昇速度が遅いことがわかる。また微細気泡の気泡径と気泡の上昇時間の関係を示したのが図10のグラフである。このグラフは横軸が気泡径(μm)で縦軸が30cm上昇時間(分)であり、気泡径が小さい程上昇時間が遅いことがわかる。このことから、気泡径が小さい程、浴槽1内に滞留する時間が長くなり、酸素富化空気の酸素が浴水Wに多く溶解することとなる。   As described above, by supplying the oxygen-enriched air generated in the oxygen-enriching device 2a to the ejector 10 of the micro-bubble generating device 3, the micro-bubbles of the oxygen-enriched air can be generated. The diameter is desirably 200 nm to 100 μm. By the way, the graph of FIG. 9 shows the relationship between the bubble diameter of the fine bubbles and the rising speed of the bubbles. In this graph, the horizontal axis is the bubble diameter (μm) and the vertical axis is the rising speed (m / s), and it can be seen that the smaller the bubble diameter, the slower the rising speed of the bubbles. Further, the graph of FIG. 10 shows the relationship between the bubble diameter of the fine bubbles and the rising time of the bubbles. In this graph, the horizontal axis is the bubble diameter (μm) and the vertical axis is the 30 cm rise time (minutes), and the rise time is slower as the bubble diameter is smaller. For this reason, the smaller the bubble diameter, the longer the residence time in the bathtub 1, and the more oxygen in the oxygen-enriched air is dissolved in the bath water W.

微細気泡の気泡径は小さくする程、浴槽1内への滞留時間が長くて溶解する酸素の量が多くなるのであるが、200nm以下の気泡を実現するためには浴水Wに電解質を投与する必要があり、不便且つ機器の腐食等を配慮する必要がある。このため気泡径の下限を200nmとしている。また浴槽1内に微細気泡を吐出する吐出口23の位置と浴槽1の水面との高さを30cmとした場合、浴水Wへの酸素の溶解に必要な時間である1分を満足するには100μm以下の気泡径が必要である。これ以上の気泡径であると、泡がそのまま上昇して溶解には寄与しない。このために気泡径の上限を100μmとしている。さらに気泡径が70μm以下であると、2分以上滞留するのでより溶解効果が得られる。   The smaller the bubble diameter of the fine bubbles, the longer the residence time in the bathtub 1 and the greater the amount of dissolved oxygen. In order to realize bubbles of 200 nm or less, an electrolyte is administered to the bath water W. It is necessary to consider inconvenience and corrosion of equipment. For this reason, the lower limit of the bubble diameter is set to 200 nm. Moreover, when the height of the position of the discharge port 23 for discharging fine bubbles into the bathtub 1 and the water surface of the bathtub 1 is 30 cm, 1 minute, which is the time required for dissolving oxygen in the bath water W, is satisfied. Requires a bubble diameter of 100 μm or less. When the bubble diameter is larger than this, the bubbles rise as they are and do not contribute to dissolution. For this reason, the upper limit of the bubble diameter is set to 100 μm. Further, when the bubble diameter is 70 μm or less, the solution stays for 2 minutes or more, so that a dissolution effect is obtained.

また微細気泡を発生しているときの運転時間と浴水Wへの酸素溶存量の関係を示すのが図7のグラフである。このグラフは横軸が運転時間(分)であり、縦軸が溶存酸素量(ml/L)である。これは浴槽1内の湯温を約40.5℃とし、湯の量を200リットルとし、0.5リットル/minの空気を微細気泡発生装置3に供給して微細気泡を発生させて酸素溶存量を測定したものである。このとき、微細気泡の気泡径の分布は図11のグラフの通りである。このグラフで横軸に気泡径(μm)、縦軸に頻度(%)を示す。   FIG. 7 is a graph showing the relationship between the operation time when fine bubbles are generated and the amount of dissolved oxygen in the bath water W. In this graph, the horizontal axis represents the operation time (minutes), and the vertical axis represents the dissolved oxygen amount (ml / L). The hot water temperature in the bathtub 1 is about 40.5 ° C., the amount of hot water is 200 liters, 0.5 liter / min of air is supplied to the fine bubble generator 3 to generate fine bubbles, and oxygen is dissolved. The amount is measured. At this time, the distribution of the bubble diameters of the fine bubbles is as shown in the graph of FIG. In this graph, the horizontal axis represents the bubble diameter (μm), and the vertical axis represents the frequency (%).

図7のグラフで符号aに示す線は室温24.4℃で、酸素濃度30%の酸素富化空気の微細気泡を形成した場合を示し、符号bに示す線は室温27.0℃で酸素濃度30%の酸素富化空気の微細気泡を形成した場合を示し、符号cに示す線は室温24.4℃、浴水Wの湯温度が40.5℃で、酸素富化空気を供給せず且つ微細気泡も発生させない通常の浴槽における浴水Wにおける溶存酸素量を示す。この図7から明らかなように、酸素富化空気を供給せず且つ微細気泡も発生させない通常の浴槽における浴水Wでは溶存酸素量は約6.3ml/Lであり、時間が経過しても変化は見られない。これに対して酸素富化空気を浴水W中に供給するものでは、酸素富化空気を浴水W中に供給して時間が経過すると共に溶存酸素量が徐々に増えていき、符号aで示す線で示される例では約2分30秒程度で溶存酸素量が7ml/Lを超え、符号bで示すものは約6分で溶存酸素量が7ml/Lを超えることがわかる。   In the graph of FIG. 7, the line indicated by the symbol a indicates a case where fine bubbles of oxygen-enriched air having an oxygen concentration of 30% are formed at a room temperature of 24.4 ° C., and the line indicated by the symbol b indicates an oxygen at a room temperature of 27.0 ° C. The case where fine bubbles of oxygen-enriched air having a concentration of 30% are formed is shown. The line indicated by the symbol c is a room temperature of 24.4 ° C. and the temperature of the bath water W is 40.5 ° C., and oxygen-enriched air is supplied. It shows the amount of dissolved oxygen in the bath water W in a normal bathtub that does not generate fine bubbles. As is apparent from FIG. 7, the amount of dissolved oxygen is about 6.3 ml / L in the bath water W in a normal bath that does not supply oxygen-enriched air and does not generate fine bubbles. There is no change. In contrast, when oxygen-enriched air is supplied into the bath water W, the oxygen-enriched air is supplied into the bath water W and the amount of dissolved oxygen gradually increases as time passes. In the example shown by the line shown, it can be seen that the dissolved oxygen amount exceeds 7 ml / L in about 2 minutes and 30 seconds, and the dissolved oxygen amount exceeds 7 ml / L in about 6 minutes in the case indicated by symbol b.

図8のグラフは、湯上り後における人の皮膚の角質の水分量変化を示すグラフである。図8において符号dで示す線は、図7において、符号aの線で示される室温24.4℃、湯温度40.5℃で、酸素濃度30%の酸素富化空気の微細気泡を形成した浴水W中に、被験者(成人女性)が図7の5分から15分の間の10分間(つまり浴水W中の溶存酸素量が約7.5ml/Lから約9.2ml/Lとなるまでの10分間)だけ入浴し、入浴終了後における角質の水分量変化(実験をした被験者は16名でその平均変化量)を示している。また、図8において符号eで示す線は、上記同じ16名の被験者が、それぞれ別の日のほぼ同じ時刻に室温24.4℃、湯温度40.5℃で且つ酸素富化空気を供給しない通常の浴水W中に10分間だけ入浴し、入浴終了後における角質の水分量変化(16名の被験者の平均変化量)を示している。なお、被験者はいずれもやや乾燥肌の人であり、入浴前の角質水分量は40μsであった。   The graph in FIG. 8 is a graph showing a change in the amount of moisture in the keratin of human skin after bathing. In FIG. 8, the line indicated by symbol d formed fine bubbles of oxygen-enriched air having an oxygen concentration of 30% at room temperature of 24.4 ° C. and hot water temperature of 40.5 ° C. indicated by the symbol a in FIG. In the bath water W, the subject (adult female) becomes 10 minutes between 5 minutes and 15 minutes in FIG. 7 (that is, the amount of dissolved oxygen in the bath water W is about 7.5 ml / L to about 9.2 ml / L). 10 minutes) until the end of the bathing, the change in the amount of horny water (the number of subjects who experimented was 16 and the average amount of change). Further, the line indicated by symbol e in FIG. 8 indicates that the same 16 subjects do not supply oxygen-enriched air at room temperature 24.4 ° C. and hot water temperature 40.5 ° C. at approximately the same time on different days. The figure shows the change in the amount of water in the keratin after taking the bath for 10 minutes in normal bath water W (average change in 16 subjects). In addition, all the subjects were people with slightly dry skin, and the amount of keratin moisture before bathing was 40 μs.

この図8のグラフから明らかなように、符号eに示す線で表される通常の浴水W(浴水Wの溶存酸素量が約6.3ml/L)に入浴した場合は、角質水分量が湯上り直後200μmであったのが、湯上り後、約12分で50μmに低下して乾燥した肌となったが、符号dに示す線で表される酸素富化空気を浴水Wに供給して浴水W中の溶存酸素量が約7.5ml/Lから約9.2ml/Lとなるまでの10分間入浴した場合は、角質水分量が湯上り直後200μmから50μmに低下するのに約32分かかり、浴水中の溶存酸素量が多い方が角質水分量の低下に要する時間を長く延ばすことができることが判明する。   As is apparent from the graph of FIG. 8, when bathing in the normal bath water W (the dissolved oxygen amount of the bath water W is about 6.3 ml / L) represented by the line indicated by the symbol e, the amount of horny water However, it was 200 μm immediately after pouring, and after 12 pours, the skin decreased to 50 μm in about 12 minutes and became dry skin. However, oxygen-enriched air represented by the line indicated by symbol d was supplied to the bath water W. When bathing for 10 minutes until the amount of dissolved oxygen in the bath water W is about 7.5 ml / L to about 9.2 ml / L, the amount of stratum corneum decreases from 200 μm to 50 μm immediately after bathing. It turns out that the time required for the decrease in the amount of stratum corneum can be extended longer when the amount of dissolved oxygen in the bath water is larger.

このように、浴水中の溶存酸素量が多い方が角質水分量の低下に要する時間を長く延ばすことができるので、湯上り後に肌の湿った状態を長く維持できて、化粧水などにより肌の手入れを余裕を持って行うことができるものであり、保湿効果を高めて肌をしっとりさせ、化粧ののりを良くすることができることになる。   In this way, the amount of dissolved oxygen in the bath water can prolong the time required to reduce the amount of keratinous moisture, so that the skin can be kept moist after bathing, and the skin can be maintained with lotion. Can be performed with a margin, and the moisturizing effect can be enhanced to moisturize the skin and improve the makeup paste.

上記のように、普通の浴水に比べて溶存酸素量が高い浴水中に入浴した場合に角質の水分保持能力が向上して角質水分量の低下に要する時間が長くなるのは以下の理由によると考えられている。すなわち、浴槽1内の浴水W中の溶存酸素濃度が高くなると、人の皮膚の角質の酸素分圧より浴水Wの酸素分圧が高くなり、身体の浴水W中の部位において浸透圧が生じて水分浸透が促進され、また高濃度の溶存酸素が角質内天然保湿因子(NMF)に作用し、水分保持能力を向上させ、また高濃度の溶存酸素が角質内の細胞間脂質に作用し、水分保持能力を向上させる。これらの理由により、湯上り後における角質の水分量の低下に要する時間を長く延ばすことができると考えられる。   As described above, when bathing in bath water having a higher dissolved oxygen amount than normal bath water, the water retention capacity of the keratin is improved and the time required for the decrease in the amount of keratin water is increased due to the following reason. It is believed that. That is, when the dissolved oxygen concentration in the bath water W in the bathtub 1 increases, the oxygen partial pressure of the bath water W becomes higher than the oxygen partial pressure of the horny skin of the human skin, and the osmotic pressure at the site in the body bath water W. Water penetration is promoted, and high concentration of dissolved oxygen acts on the natural moisturizing factor (NMF) in the stratum corneum, improving water retention capacity, and high concentration of dissolved oxygen acts on intercellular lipids in the stratum corneum. And improve the water retention capacity. For these reasons, it is considered that the time required for the decrease in the amount of moisture in the keratin after bathing can be extended.

ここで、浴槽1の浴水W中の溶存酸素量が7ml/Lに満たないと、角質水分量の低下に要する時間が普通の浴水Wの場合とさほど変わらず、湯上り後に肌の湿った状態を長く維持できなくて、余裕を持って肌が湿った状態で化粧水などにより肌の手入れができないので好ましくない。また、浴槽1の浴水W中の溶存酸素量が13ml/Lを超えると、浴水面から浴室空間内に多量の富化酸素が放出され、浴室空間内における酸素濃度が必要以上に高くなって、入浴している人の身体に対する負担が大きくて好ましくない。このため、本発明においては、浴水中の溶存酸素量を7ml/L〜13ml/L、好ましくは7.5ml/L〜12ml/Lとしている。   Here, if the amount of dissolved oxygen in the bath water W of the bathtub 1 is less than 7 ml / L, the time required for the decrease in the amount of keratin moisture is not so different from that of the ordinary bath water W, and the skin becomes damp after bathing. Since the state cannot be maintained for a long time and the skin is moist with sufficient margin, skin care cannot be performed with a lotion or the like. Moreover, when the amount of dissolved oxygen in the bath water W of the bathtub 1 exceeds 13 ml / L, a large amount of enriched oxygen is released from the bath water surface into the bathroom space, and the oxygen concentration in the bathroom space becomes higher than necessary. The burden on the body of the person taking a bath is large, which is not preferable. For this reason, in the present invention, the amount of dissolved oxygen in the bath water is 7 ml / L to 13 ml / L, preferably 7.5 ml / L to 12 ml / L.

浴水中の溶存酸素量を7ml/L〜13ml/Lにするに当たっては、上記した実施形態では、酸素富化空気供給手段2や微細気泡発生装置3の能力、浴槽1内に張る浴水の湯量、湯温、室温等と、酸素富化空気の供給量、供給時間等との関係をあらかじめ実験により求め、これに基づいて、浴水Wを7ml/L〜13ml/Lの範囲中における目的とする溶存酸素量とするための浴水W中への酸素富化空気の供給量、供給時間等を求め、これにより、酸素富化空気供給手段2、微細気泡発生装置3の運転時間が決定される。したがって、溶存酸素量を上記7ml/L〜13ml/Lという範囲内において目的とする溶存酸素量にするに当たっては、上記に基づいて酸素富化空気供給手段2、微細気泡発生装置3の運転時間を制御部19により制御することで溶存酸素量を上記7ml/L〜13ml/Lという範囲内において目的とする溶存酸素量にすることができる。   In setting the amount of dissolved oxygen in the bath water to 7 ml / L to 13 ml / L, in the above-described embodiment, the capacity of the oxygen-enriched air supply means 2 and the fine bubble generator 3 and the amount of hot water in the bath 1 are set. The relationship between the hot water temperature, room temperature, etc., the supply amount of oxygen-enriched air, the supply time, etc. is obtained beforehand by experiment, and based on this, the purpose of bath water W in the range of 7 ml / L to 13 ml / L The amount of supply of oxygen-enriched air into the bath water W to obtain the dissolved oxygen amount, the supply time, etc. are obtained, and thereby the operation time of the oxygen-enriched air supply means 2 and the fine bubble generator 3 is determined. The Therefore, when the dissolved oxygen amount is set to the target dissolved oxygen amount within the range of 7 ml / L to 13 ml / L, the operation time of the oxygen-enriched air supply means 2 and the fine bubble generator 3 is set based on the above. By controlling by the control part 19, the dissolved oxygen amount can be made into the target dissolved oxygen amount within the range of 7 ml / L to 13 ml / L.

また、酸素富化空気供給手段2から供給される酸素富化空気の酸素濃度は25%〜40%とする。すなわち、酸素富化空気供給手段2から供給される酸素富化空気の酸素濃度が25%に満たないと、これを浴水Wに供給しても通常の一般の浴槽1内の浴水Wの溶存酸素量と殆どかわらず、目的とする溶存酸素量にすることができないので好ましくない。また、酸素富化空気供給手段2から供給される酸素富化空気の酸素濃度が40%を超えると、浴水Wに溶け切らずに水面から浴室6空間内に放出される酸素富化空気の量が多くなり、浴室6空間内の酸素濃度が必要以上に高くなって身体に対する負担が大きくて好ましくない。   Further, the oxygen concentration of the oxygen-enriched air supplied from the oxygen-enriched air supply means 2 is set to 25% to 40%. That is, when the oxygen concentration of the oxygen-enriched air supplied from the oxygen-enriched air supply means 2 is less than 25%, the bath water W in the ordinary general bath 1 is supplied to the bath water W. This is not preferable because the target dissolved oxygen amount cannot be achieved regardless of the amount of dissolved oxygen. Moreover, when the oxygen concentration of the oxygen-enriched air supplied from the oxygen-enriched air supply means 2 exceeds 40%, the oxygen-enriched air released from the water surface into the bathroom 6 space without being completely dissolved in the bath water W. The amount increases, the oxygen concentration in the bathroom 6 space becomes higher than necessary, and the burden on the body is large, which is not preferable.

ところで、上記実施形態においては、酸素富化空気を浴槽1の浴水W中に供給するに当たって、微細気泡として浴水W中に供給するので、浴槽1内に入って居る入浴者が微細気泡で包まれて温熱効果が得られ、また酸素富化空気の微細気泡で包まれるために入浴者の皮膚呼吸を促進できる。これにより、入浴中の快適度を上昇できると共に心肺機能の負担を軽減できる。また疲労回復(筋肉中の乳酸が酸素により分解される作用が促進される)されると共に皮膚の活性化がされ、さらに肌の保湿性が向上される。   By the way, in the said embodiment, when supplying oxygen enriched air in the bath water W of the bathtub 1, since it supplies in the bath water W as a fine bubble, the bather who is in the bathtub 1 is a fine bubble. Wrapped to provide a thermal effect, and because it is wrapped with fine bubbles of oxygen-enriched air, it can promote bather skin respiration. Thereby, the comfort level during bathing can be increased and the burden of cardiopulmonary function can be reduced. In addition, recovery from fatigue (accelerating the action of lactic acid in the muscles being decomposed by oxygen) and activation of the skin, further improving the moisture retention of the skin.

なお、酸素富化装置2aから供給される酸素富化空気の流量は微細気泡発生装置3で使用される流量より多くなるように設定し、余剰の酸素富化空気を浴室6内に供給するようにしてもよい。これにより浴室6内の空気の酸素濃度が上がり、肺呼吸を楽にして快適に入浴できる。   Note that the flow rate of the oxygen-enriched air supplied from the oxygen-enriching device 2a is set to be larger than the flow rate used in the fine bubble generating device 3, so that excess oxygen-enriched air is supplied into the bathroom 6. It may be. As a result, the oxygen concentration of the air in the bathroom 6 is increased, and the lungs can be easily relieved and bathed comfortably.

また、本実施形態において、酸素富化空気供給手段2から供給される酸素富化空気を浴槽1内の浴水Wに供給するのに加え、酸素富化空気供給手段2から供給される酸素富化空気の一部を浴室6空間内に供給するようにしてもよい。この場合、浴室6内の空気の酸素濃度が上がり、肺呼吸を楽にして快適に入浴することが可能となる。   In this embodiment, in addition to supplying the oxygen-enriched air supplied from the oxygen-enriched air supply unit 2 to the bath water W in the bathtub 1, the oxygen-enriched air supplied from the oxygen-enriched air supply unit 2 A part of the chemical air may be supplied into the bathroom 6 space. In this case, the oxygen concentration of the air in the bathroom 6 increases, and it becomes possible to take a comfortable bath with ease of lung respiration.

図3乃至図6には本発明の他の実施形態を示している。この実施形態では前述のように酸素富化空気供給手段2から供給された酸素富化空気を微細気泡として浴槽1の浴水W中に供給する微細気泡発生装置3に加えて、更に浴槽1内から吸い込んだ浴水Wに空気を巻き込むと共に空気を巻き込んだ気泡入りの浴水Wを浴槽1内に噴出するジェットバス装置22を設けたものである。   3 to 6 show another embodiment of the present invention. In this embodiment, in addition to the fine bubble generating device 3 for supplying oxygen-enriched air supplied from the oxygen-enriched air supply means 2 as fine bubbles into the bath water W of the bathtub 1 as described above, A jet bath device 22 is provided for entraining air into the bath water W sucked in from the air and jetting the bubble bath water W entrained with air into the bathtub 1.

ジェットバス装置22は吸い込み口13と噴出口14と循環管路9とジェットポンプ17と空気取り込み口24と空気供給管路16とで主体が構成されている。浴槽1の側壁には吸い込み口13を装着してあり、浴槽1内の浴水Wを吸い込むようになっている。また浴槽1の側壁には噴出口14を設けてあり、噴出口14から比較的大きな気泡を含んだ浴水Wを噴出するようになっている。吸い込み口13と噴出口14との間は浴槽1外に配管した循環管路9にて連通させてあり、循環管路9の途中にはジェットポンプ17を配置してあり、ジェットポンプ17を駆動することにより吸い込み口14から吸い込んだ浴水Wを噴出口14から強く噴出するようになっている。浴槽1のフランジ18には空気取り込み口24を設けてあり、この空気取り込み口24と噴出口14とを連通させてある。そして噴出口14にはエジェクター部を設けてあり、噴出口14から浴水Wを噴出することで空気取り込み口24から取り込んだ空気を浴水Wに巻き込み、比較的大きな気泡を含んだ浴水Wを噴出するようになっている。また、図3に示すように、浴槽1のフランジ18には微細気泡発生装置3の操作スイッチ20に加え、ジェットバス装置22の操作スイッチ21を設けている。   The jet bath device 22 is mainly composed of a suction port 13, a jet port 14, a circulation line 9, a jet pump 17, an air intake port 24, and an air supply line 16. A suction port 13 is attached to the side wall of the bathtub 1, and the bath water W in the bathtub 1 is sucked in. Moreover, the jet nozzle 14 is provided in the side wall of the bathtub 1, and the bath water W containing the comparatively big bubble is jetted from the jet nozzle 14. FIG. The suction port 13 and the jet port 14 are communicated with each other through a circulation line 9 piped outside the bathtub 1, and a jet pump 17 is arranged in the middle of the circulation line 9 to drive the jet pump 17. By doing so, the bath water W sucked from the suction port 14 is strongly ejected from the spout 14. The flange 18 of the bathtub 1 is provided with an air intake port 24, and the air intake port 24 and the jet port 14 are communicated with each other. The ejector port 14 is provided with an ejector, and the air taken in from the air intake port 24 is engulfed in the bath water W by ejecting the bath water W from the jet port 14, and the bath water W containing relatively large bubbles. Is supposed to spout. As shown in FIG. 3, the flange 18 of the bathtub 1 is provided with an operation switch 21 of the jet bath device 22 in addition to the operation switch 20 of the fine bubble generating device 3.

ここで、図5、図6に示すように酸素富化装置2aで得られた酸素富化空気を供給する空気供給経路4を2つの分岐経路4a,4bに分岐し、一方の分岐経路4aを微細気泡発生装置3のエジェクター10に連通させ、他方の分岐経路4bを空気取り込み口24に連通させるようにしてもよい。この場合、酸素富化装置2aで得られる酸素富化空気の量が例えば2リットル/minであり、微細気泡発生装置3のエジェクター10で取り入れられる酸素富化空気が0.5リットル/minであると、空気取り込み口24に1.5リットル/minの酸素富化空気が供給されるようにする。したがって、図5のようにジェットバス装置22を運転せず、微細気泡発生装置3のみを運転する場合、空気取り込み口24から浴室6空間内に1.5リットル/minの酸素富化空気が供給され、微細気泡発生装置3側に0.5リットル/minの酸素富化空気が供給されて微細気泡となって浴槽1内の浴水W中に供給される。また、微細気泡発生装置3を運転せず、ジェットバス装置22を運転すると、空気取り込み口24から浴室6空間内の空気が吸い込まれると共に2リットル/minの空気が空気取り込み口24側に供給されて上記空気取り込み口24と共に噴出口14にはエジェクター部に吸い込まれ、噴出口14から比較的大きな気泡を含んだ浴水Wを噴出し、入浴者をジェット水でマッサージすることができる。この際、空気取り込み口24から空気を取り込むとき、空気取り込み口24に酸素富化空気が供給されているために酸素富化空気を含んだ気泡が噴出される。これにより酸素富化空気が入浴者の顔面付近に漂い、肺呼吸を楽にして快適に入浴することができる。   Here, as shown in FIGS. 5 and 6, the air supply path 4 for supplying oxygen-enriched air obtained by the oxygen enricher 2a is branched into two branch paths 4a and 4b, and one branch path 4a is You may make it connect with the ejector 10 of the microbubble generator 3, and make the other branch path | route 4b connect with the air intake port 24. FIG. In this case, the amount of oxygen-enriched air obtained by the oxygen-enriching device 2a is, for example, 2 liter / min, and the oxygen-enriched air taken in by the ejector 10 of the fine bubble generating device 3 is 0.5 liter / min. Then, 1.5 liter / min of oxygen-enriched air is supplied to the air intake port 24. Accordingly, when the jet bath device 22 is not operated as shown in FIG. 5 and only the fine bubble generating device 3 is operated, oxygen-enriched air of 1.5 liter / min is supplied from the air intake port 24 into the bathroom 6 space. Then, 0.5 liter / min of oxygen-enriched air is supplied to the fine bubble generating device 3 side, and the fine bubbles are supplied into the bath water W in the bathtub 1. Further, when the jet bath device 22 is operated without operating the fine bubble generating device 3, air in the bathroom 6 space is sucked from the air intake port 24 and air of 2 liters / min is supplied to the air intake port 24 side. Thus, the jet port 14 together with the air intake port 24 is sucked into the ejector section, and the bath water W containing relatively large bubbles is ejected from the jet port 14 so that the bather can be massaged with jet water. At this time, when the air is taken in from the air intake port 24, since the oxygen-enriched air is supplied to the air intake port 24, bubbles containing the oxygen-enriched air are ejected. As a result, oxygen-enriched air drifts in the vicinity of the bather's face, so that the patient can take a comfortable bath with ease of lung respiration.

この場合、ジェットバス装置22で供給すると気泡が比較的大きいため、酸素富化空気は浴槽1内の浴水W中における滞留時間がきわめて短く、ジェットバス装置22の運転のみでは浴水W中の溶存酸素量を上記7ml/L〜13ml/Lにすることは難しい。したがって、ジェットバス装置22の運転の後で、微細気泡発生装置3の運転を行ったり、あるいは、微細気泡発生装置3の運転を行った後にジェットバス装置22の運転をおこなったり、あるいは、微細気泡発生装置3の運転と、ジェットバス装置22の運転を交互にしたり、あるいは、同時にしたりすることで、浴槽1内の浴水Wの溶存酸素量を7ml/L〜13ml/Lにするとよい。   In this case, since the bubbles are relatively large when supplied by the jet bath device 22, the residence time of the oxygen-enriched air in the bath water W in the bathtub 1 is extremely short. It is difficult to make the dissolved oxygen amount 7 ml / L to 13 ml / L. Therefore, after the operation of the jet bath device 22, the micro bubble generator 3 is operated, or after the micro bubble generator 3 is operated, the jet bath device 22 is operated, or the micro bubbles It is preferable that the amount of dissolved oxygen in the bath water W in the bathtub 1 is set to 7 ml / L to 13 ml / L by alternately operating the generator 3 and the operation of the jet bath device 22 or simultaneously.

本発明の実施の形態の一例を示す一部切欠斜視図である。It is a partially cutaway perspective view showing an example of an embodiment of the present invention. 同上の微細気泡発生装置の動作を説明する説明図である。It is explanatory drawing explaining operation | movement of a microbubble generator same as the above. 本発明の他の実施の形態の一例を示す一部切欠斜視図である。It is a partially cutaway perspective view showing an example of another embodiment of the present invention. 同上の浴槽部分の斜視図である。It is a perspective view of a bathtub part same as the above. 同上の微細気泡発生装置の動作を説明する説明図である。It is explanatory drawing explaining operation | movement of a microbubble generator same as the above. 同上のジェットバス装置の動作を説明する説明図である。It is explanatory drawing explaining operation | movement of a jet bath apparatus same as the above. 浴水中に酸素富化空気を供給した場合と酸素富化空気を供給しない普通の浴水中における溶存酸素量と時間との関係を示すグラフである。It is a graph which shows the relationship between the amount of dissolved oxygen and the time in the normal bath water which does not supply oxygen enriched air when oxygen enriched air is supplied in bath water. 浴水中に酸素富化空気を供給して溶存酸素量が多くなった浴水に入浴した場合と酸素富化空気を供給しない普通の浴水に入浴した場合の湯上り後における角質の水分量変化を示すグラフである。Changes in the amount of horny water after bathing when bathing in bath water with a high dissolved oxygen content by supplying oxygen-enriched air into bath water and bathing in normal bath water without supplying oxygen-enriched air It is a graph to show. 微細気泡の気泡径と気泡の上昇速度の関係を示すグラフである。It is a graph which shows the relationship between the bubble diameter of a fine bubble, and the bubble rising speed. 微細気泡の気泡径と気泡の上昇時間の関係を示すグラフである。It is a graph which shows the relationship between the bubble diameter of a fine bubble, and the bubble rising time. 微細気泡の気泡径の分布を示すグラフである。It is a graph which shows distribution of the bubble diameter of a fine bubble.

符号の説明Explanation of symbols

1 浴槽
2 酸素富化空気供給手段
3 微細気泡発生装置
DESCRIPTION OF SYMBOLS 1 Bath 2 Oxygen-enriched air supply means 3 Fine bubble generator

Claims (3)

空気中の酸素濃度よりも高濃度の酸素を含む酸素富化空気を浴槽内の浴水中に供給する酸素富化空気供給手段を設け、該酸素富化空気供給手段による酸素富化空気の浴槽内の浴水中への供給により浴水中の溶存酸素量を7ml/L〜13ml/Lとすることを特徴とする浴槽装置。   There is provided oxygen-enriched air supply means for supplying oxygen-enriched air containing oxygen at a concentration higher than the oxygen concentration in the air into the bath water in the bath, and the oxygen-enriched air in the bathtub by the oxygen-enriched air supply means A bath apparatus characterized in that the amount of dissolved oxygen in the bath water is 7 ml / L to 13 ml / L by supplying the bath water into the bath water. 前記酸素富化空気供給手段からの酸素富化空気の供給を受けて浴水に酸素富化空気からなる微細気泡を発生する微細気泡発生装置を備えたことを特徴とする請求項1記載の浴槽装置。   2. The bathtub according to claim 1, further comprising a fine bubble generating device that receives supply of oxygen-enriched air from the oxygen-enriched air supply means and generates fine bubbles made of oxygen-enriched air in the bath water. apparatus. 酸素富化空気供給手段から供給される酸素富化空気の酸素濃度が25%〜40%であることを特徴とする請求項1又は請求項2記載の浴槽装置。
The bathtub apparatus according to claim 1 or 2, wherein the oxygen concentration of the oxygen-enriched air supplied from the oxygen-enriched air supply means is 25% to 40%.
JP2004381387A 2004-12-28 2004-12-28 Bathtub apparatus Pending JP2006181290A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011088080A (en) * 2009-10-23 2011-05-06 Tomotaka Marui Microbubble-containing composition and microbubble generator
CN108498314A (en) * 2018-02-28 2018-09-07 佛山市熙华科技有限公司 A kind of clipping oxygen bubble beautifying apparatus
JP2020081408A (en) * 2018-11-27 2020-06-04 政安 宮崎 Electric heater built-in heat insulating bathtub and unit bath

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH042347A (en) * 1990-04-14 1992-01-07 Matsushita Electric Works Ltd Apparatus for supplying oxygen into bath tub
JPH04295359A (en) * 1991-03-22 1992-10-20 Toto Ltd Device for bathtub
JPH0824606A (en) * 1994-07-11 1996-01-30 Nippon Gijutsu Kaihatsu Center:Kk Apparatus for automatic generation of water containing fine air bubble
JP2004350932A (en) * 2003-05-29 2004-12-16 Matsushita Electric Ind Co Ltd Oxygen enrichment water heater

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH042347A (en) * 1990-04-14 1992-01-07 Matsushita Electric Works Ltd Apparatus for supplying oxygen into bath tub
JPH04295359A (en) * 1991-03-22 1992-10-20 Toto Ltd Device for bathtub
JPH0824606A (en) * 1994-07-11 1996-01-30 Nippon Gijutsu Kaihatsu Center:Kk Apparatus for automatic generation of water containing fine air bubble
JP2004350932A (en) * 2003-05-29 2004-12-16 Matsushita Electric Ind Co Ltd Oxygen enrichment water heater

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011088080A (en) * 2009-10-23 2011-05-06 Tomotaka Marui Microbubble-containing composition and microbubble generator
CN108498314A (en) * 2018-02-28 2018-09-07 佛山市熙华科技有限公司 A kind of clipping oxygen bubble beautifying apparatus
JP2020081408A (en) * 2018-11-27 2020-06-04 政安 宮崎 Electric heater built-in heat insulating bathtub and unit bath
JP7240860B2 (en) 2018-11-27 2023-03-16 政安 宮崎 A unit bath equipped with a hot tub with built-in electric heater and a hot tub with built-in electric heater

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