JP2005110913A - Oxygen enriched hot water supply device - Google Patents

Oxygen enriched hot water supply device Download PDF

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JP2005110913A
JP2005110913A JP2003348205A JP2003348205A JP2005110913A JP 2005110913 A JP2005110913 A JP 2005110913A JP 2003348205 A JP2003348205 A JP 2003348205A JP 2003348205 A JP2003348205 A JP 2003348205A JP 2005110913 A JP2005110913 A JP 2005110913A
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oxygen
air
hot water
enriched
mixing
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Kentaro Sahashi
賢太郎 佐橋
Hirofumi Kawashima
裕文 河島
Norio Sugawara
範夫 菅原
Kazuhito Uehara
一仁 上原
Masaki Sugiyama
正樹 杉山
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Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a means for preventing dew generated in the oxygen mixing operation from remaining in an oxygen supply passage. <P>SOLUTION: The oxygen enriched hot water supply device comprises a reheating circulating circuit 20 for circulating hot water in a bathtub 21 by a circulating pump 18, a reheating adaptor 22 mounted on the bathtub 21, an oxygen enriching device 26 for letting air permeate an oxygen enriching film 23 by a decompression means 24 and taking out high-concentration oxygen, and a mixing means 27 for mixing the high-concentration oxygen from the oxygen enriching device 26 to the reheating circulating circuit 20. The high-concentration oxygen mixed in circulation water is jetted out of an outlet of the reheating adaptor 22. The oxygen enriched hot water supply device also has air selecting valves 29 and 30 to form atmospheric air releasing passages between the oxygen enriching film 23 and the decompression means 24 and between the decompression means 24 and the mixing means 27, so that dew, remaining in the oxygen supply passage because of the suction of steam generated when the oxygen mixing operation is continued for a long period of time, is discharged. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は追焚き循環回路を有する給湯器の追焚き配管を利用して、浴槽内の浴水中に酸素を供給する機能を有する給湯装置に関するものである。   The present invention relates to a hot water supply apparatus having a function of supplying oxygen into bath water in a bathtub using a reheating pipe of a water heater having a recirculation circuit.

従来この種の酸素供給装置は、微細気泡発生装置やジェット噴射装置を取り付け、この各装置を介して浴槽水を循環させる泡風呂やジェットバス等の浴槽水を循環させる管路に気体を供給する供給部を設け、この供給部に酸素富化空気を供給するための酸素富化装置を設けたものである(例えば、特許文献1参照)。   Conventionally, this type of oxygen supply device is equipped with a fine bubble generator or jet injection device, and supplies gas to a pipeline for circulating bath water such as a bubble bath or jet bath that circulates bath water through these devices. A supply unit is provided, and an oxygen enricher for supplying oxygen-enriched air to the supply unit is provided (see, for example, Patent Document 1).

図3は、上記公報に記載された従来の浴槽内への酸素供給装置を示すものである。図において、1は浴槽、2は管路、3は供給部、4は吸入口、5は吐出口、7は酸素富化装置、8はポンプである。
特開平4−2347号公報
FIG. 3 shows an oxygen supply device for a conventional bathtub described in the above publication. In the figure, 1 is a bathtub, 2 is a conduit, 3 is a supply section, 4 is a suction port, 5 is a discharge port, 7 is an oxygen enrichment device, and 8 is a pump.
JP-A-4-2347

上記従来の構成では、連続運転を長時間続けると酸素富化装置は空気と共に水蒸気も取り込んで、その吸い込んだ水蒸気が酸素富化膜を透過して酸素供給経路となる配管内に結露水として残留するという問題点があり、この残留結露水により雑菌の増加や低温時における凍結等の不具合に繋がるという課題を有していた。   In the above conventional configuration, when continuous operation is continued for a long time, the oxygen enricher takes in water vapor together with air, and the sucked water vapor passes through the oxygen enriched film and remains as condensed water in the pipe serving as the oxygen supply path. There is a problem that the residual dew condensation water leads to problems such as increase of various germs and freezing at low temperatures.

本発明は上記従来の課題を解決するもので、酸素混入運転により生成される結露水が酸素供給経路に残留することを回避する手段を提供することを目的としたものである。   SUMMARY OF THE INVENTION The present invention solves the above-described conventional problems, and an object of the present invention is to provide means for avoiding that dew condensation water generated by an oxygen mixing operation remains in an oxygen supply path.

上記従来の課題を解決するため本発明の酸素富化給湯装置は、循環ポンプにより浴槽の湯を循環する追い焚き循環回路と、前記浴槽に設けた追い焚きアダプタと、減圧手段により酸素富化膜に空気を通過させることにより高濃度の酸素を取出す酸素富化装置と、前記酸素富化装置からの高濃度の酸素を追い焚き循環回路に混入させる混入手段とを有し、前記追焚きアダプタの噴出口より循環水に混入させた高濃度の酸素を噴出させる構成としたものであって、前記酸素富化膜と減圧手段の間及び減圧手段と混入手段との間に大気開放経路が形成可能となる空気切り替え弁を備えた構成としてある。   In order to solve the above-described conventional problems, an oxygen-enriched hot water supply apparatus of the present invention includes a recirculation circuit that circulates hot water in a bathtub by a circulation pump, a reheating adapter provided in the bathtub, and an oxygen-enriched film by a decompression unit. An oxygen enrichment device that takes out high concentration oxygen by passing air through, and a mixing means for mixing high concentration oxygen from the oxygen enrichment device into a recirculation circuit, A high-concentration oxygen mixed into the circulating water is jetted from the jet outlet, and an open air path can be formed between the oxygen-enriched film and the pressure-reducing means and between the pressure-reducing means and the mixing means. It is set as the structure provided with the air switching valve used.

これによって、酸素混入運転後に酸素供給経路に残留してある結露水を器具外に排出、若しくは乾燥空気により自然蒸発させることが出来るので、残留結露水による雑菌の増加や低温時における凍結等の問題を解消することができる。   As a result, the condensed water remaining in the oxygen supply path after the oxygen mixing operation can be discharged out of the apparatus or evaporated spontaneously with dry air, so there are problems such as increase of bacteria due to residual condensed water and freezing at low temperatures. Can be eliminated.

本発明の酸素富化給湯装置は、酸素混入運転により配管内に残留した結露水を、空気切り替え弁の切替制御により大気開放状態で減圧手段を作動させることにより、排出、乾燥することができ、残留結露水による凍結破壊、雑菌類の増殖を防ぐことができる。   The oxygen-enriched hot water supply apparatus of the present invention can discharge and dry the condensed water remaining in the pipe by the oxygen mixing operation by operating the pressure reducing means in an open state by switching control of the air switching valve. It can prevent freezing destruction and growth of miscellaneous fungi due to residual dew condensation water.

第1の発明は、循環ポンプにより浴槽の湯を循環する追い焚き循環回路と、前記浴槽に設けた追い焚きアダプタと、減圧手段により酸素富化膜に空気を通過させることにより高濃度の酸素を取出す酸素富化装置と、前記酸素富化装置からの高濃度の酸素を追い焚き循環回路に混入させる混入手段とを有し、前記追焚きアダプタの噴出口より循環水に混入させた高濃度の酸素を噴出させる構成としたものであって、前記酸素富化膜と減圧手段の間及び減圧手段と混入手段との間に大気開放経路が形成可能となる空気切り替え弁を備えたことを特徴とするものであり、酸素混入運転を連続で長時間続けた場合に生じる水蒸気の吸い込みによる酸素供給経路の配管内に結露水が残留する現象を前記酸素富化膜と減圧手段の間及び減圧手段と混入手段との間に配設した空気切替弁を制御することで、酸素供給経路が大気開放経路となるようにし、配管内に残留した結露水を排出、乾燥させるようにしたものである。   According to a first aspect of the present invention, a recirculation circuit that circulates hot water in a bathtub by a circulation pump, a reheating adapter provided in the bathtub, and high-concentration oxygen by passing air through an oxygen-enriched film by a decompression unit. An oxygen enriching device to be taken out, and a mixing means for mixing the high concentration oxygen from the oxygen enriching device into the recirculation circuit, and the high concentration mixed into the circulating water from the outlet of the reheating adapter. It is configured to eject oxygen, and includes an air switching valve capable of forming an air release path between the oxygen-enriched film and the decompression unit and between the decompression unit and the mixing unit. The phenomenon in which condensed water remains in the piping of the oxygen supply path due to the inhalation of water vapor that occurs when the oxygen-mixing operation is continued for a long time continuously, between the oxygen-enriched film and the decompression means, and the decompression means, Mixing means By controlling the air switching valve disposed between the oxygen supply path so as to be air opening path, discharging the condensed water remaining in the pipe, in which so as to dry.

第2の発明は、特に第1の発明において、高濃度の酸素を追焚き循環回路に混入させた酸素混入運転を終了した場合、空気切り替え弁を所定時間大気開放側に切り替え、減圧手段を作動させて酸素供給経路に大気を流通させるようにしたことを特徴とするものであり、酸素混入運転後に空気切替弁を酸素供給経路が大気開放経路となるように切り替え、予め定めた所定時間減圧手段を駆動させることで、酸素富化装置を経由せず、大気を直接酸素供給経路に流通させて残留した結露水を排出、乾燥させるようにしたものである。   In the second invention, particularly in the first invention, when the oxygen mixing operation in which high-concentration oxygen is added and mixed in the circulation circuit is finished, the air switching valve is switched to the atmosphere opening side for a predetermined time, and the pressure reducing means is operated. And the air switching valve is switched after the oxygen mixing operation so that the oxygen supply path becomes an air release path, and the pressure reducing means is set for a predetermined time. , By driving the air directly through the oxygen supply path without passing through the oxygen enricher, the remaining condensed water is discharged and dried.

第3の発明は、酸素富化膜に新鮮空気を供給するための送風手段を備えたことを特徴とするもので、大気から酸素富化膜を通して高濃度の酸素を取出す場合、多量の空気を酸素富化膜に供給する必要があり、ガス給湯器等に組み込んだ場合、燃焼用空気を供給するための送風ファンだけでは所望の高濃度酸素を確保することができず、そこで、酸素富化膜に新鮮空気を供給するためだけの送風手段を別途設けることで、燃焼用空気とは別に酸素富化膜に多量の新鮮空気を供給することができる。   The third invention is characterized by comprising a blowing means for supplying fresh air to the oxygen-enriched membrane. When taking out high-concentration oxygen from the atmosphere through the oxygen-enriched membrane, a large amount of air is removed. It is necessary to supply the oxygen-enriched membrane, and when it is incorporated in a gas water heater or the like, the desired high-concentration oxygen cannot be ensured only with the blower fan for supplying combustion air. By separately providing a blowing means only for supplying fresh air to the membrane, a large amount of fresh air can be supplied to the oxygen-enriched membrane separately from the combustion air.

第4の発明は、高濃度の酸素を追焚き循環回路に混入させた酸素混入運転を終了した場合、送風手段を所定時間停止させ、酸素富化膜に空気を供給しない状態で減圧手段を作動させるようにしたことを特徴とするもので、酸素混入運転終了後に送風手段を停止させた状態で減圧手段を駆動させることにより、酸素富化膜から水蒸気等の湿気を含む空気を吸い込むことなく、パージ動作を行うことができ、酸素供給経路内の残留結露水も確実に排出、乾燥することが可能となる。   In the fourth aspect of the invention, when the oxygen mixing operation in which high-concentration oxygen is chased and mixed in the circulation circuit is finished, the blowing unit is stopped for a predetermined time, and the pressure reducing unit is operated without supplying air to the oxygen-enriched membrane. By driving the pressure reducing means in a state where the air blowing means is stopped after the oxygen mixing operation is completed, without sucking in air containing moisture such as water vapor from the oxygen-enriched film, The purge operation can be performed, and the remaining condensed water in the oxygen supply path can be reliably discharged and dried.

第5の発明は、高濃度の酸素を追焚き循環回路に混入させた酸素混入運転を終了した場合、送風手段を所定時間停止させ、減圧手段と混入手段の間に設けた空気切り替え弁を大気開放側に切り替えた状態で減圧手段を作動させるようにしたことを特徴とするもので、酸素混入運転終了後に送風手段を停止させ、減圧手段と混入手段の間に配設した空気切替弁を大気開放側に切り替えて減圧手段を駆動させることにより、酸素富化膜から水蒸気等の湿気を含む空気を吸い込むことなくパージ動作を行い、酸素供給系路内の残留結露水を排出、乾燥することが可能となる。   According to a fifth aspect of the present invention, when the oxygen mixing operation in which high-concentration oxygen is chased and mixed in the circulation circuit is terminated, the air blowing means is stopped for a predetermined time, and the air switching valve provided between the pressure reducing means and the mixing means is opened to the atmosphere. The depressurization means is operated in the state of being switched to the open side. After the oxygen mixing operation is completed, the blower means is stopped, and the air switching valve disposed between the depressurization means and the mixing means is opened to the atmosphere. By switching to the open side and driving the pressure reducing means, a purge operation can be performed without sucking air containing moisture such as water vapor from the oxygen-enriched film, and residual condensed water in the oxygen supply system can be discharged and dried. It becomes possible.

第6の発明は、高濃度の酸素を追焚き循環回路に混入させた酸素混入運転中に予め設定した所定時間を検知した場合、送風手段を所定時間停止させ、酸素富化膜に空気を供給しない状態で減圧手段を作動させるようにしたことを特徴とするもので、酸素混入運転中でも予め設定した時間が経過すると、一時的に酸素混入運転を中断し、送風手段を停止した状態で減圧手段を駆動させパージ動作を行うため、確実に酸素供給経路内の残留結露水を排出、乾燥することが可能となる。   In a sixth aspect of the present invention, when a predetermined time is detected during the oxygen mixing operation in which high concentration oxygen is added to the circulation circuit and detected, the blower is stopped for a predetermined time and air is supplied to the oxygen-enriched membrane. The pressure reducing means is operated in a state in which the pressure reducing means is operated, and when the preset time has elapsed even during the oxygen mixing operation, the oxygen mixing operation is temporarily interrupted, and the pressure reducing means is stopped while the air blowing means is stopped. Since the purge operation is performed by driving the residual dew condensation water in the oxygen supply path, it is possible to reliably discharge and dry.

(実施の形態1)
図1は、本発明の第1の実施の形態における追い焚き給湯装置の全体構成図を示すものである。
(Embodiment 1)
FIG. 1 is an overall configuration diagram of a reheating hot water supply apparatus according to a first embodiment of the present invention.

図1において、給湯装置本体9の内部構成は、熱交換器12を加熱するバーナ10があり、このバーナ10に燃焼用空気を送るバーナファン11が設けられている。熱交換器12の下流側には燃焼ガスの排気口13が設けられ、バーナ10で発生した燃焼ガスを本体外に排出する。   In FIG. 1, the internal configuration of the hot water supply apparatus main body 9 includes a burner 10 that heats a heat exchanger 12, and a burner fan 11 that sends combustion air to the burner 10. A combustion gas exhaust port 13 is provided on the downstream side of the heat exchanger 12 to discharge the combustion gas generated in the burner 10 out of the main body.

また、熱交換器12には給湯入口15から入った水を加熱し給湯出口16を経由してカラン17等から吐出する給湯回路14が設けられており、さらに、前記熱交換器12には浴槽21の湯水を風呂ポンプ18で循環させ熱交換器12で加熱後、再度浴槽21に戻す追い焚き循環回路20が設けられている。   Further, the heat exchanger 12 is provided with a hot water supply circuit 14 for heating water entered from the hot water supply inlet 15 and discharging the water from the currant 17 or the like via the hot water supply outlet 16, and the heat exchanger 12 further includes a bathtub. A recirculation circuit 20 is provided that circulates the hot and cold water 21 with the bath pump 18, heats it with the heat exchanger 12, and returns it to the bathtub 21 again.

このような内部構成を有する給湯装置の一画に、大気中から酸素を取り出し高濃度化した酸素を前記追い焚き循環回路20の循環水に混入させる酸素富化装置26を配設してある。   In one section of the hot water supply apparatus having such an internal configuration, an oxygen enrichment device 26 is provided for extracting oxygen from the atmosphere and mixing the highly concentrated oxygen into the circulating water of the recirculation circuit 20.

この酸素富化装置26は、特殊な膜で構成しこの膜を空気が通過するときに酸素を取り出す酸素富化膜23と、前記酸素富化膜23に空気を通過させるとき、該空気を減圧して酸素富化膜23の間に空気を通し、高酸素濃度の空気を得るための減圧手段である真空ポンプ24と、前記酸素富化膜23に新鮮空気を供給するための送風手段である送風ファン25で構成している。   This oxygen enrichment device 26 is composed of a special membrane, and an oxygen enrichment membrane 23 for extracting oxygen when air passes through the membrane, and when the air is passed through the oxygen enrichment membrane 23, the air is decompressed. A vacuum pump 24 which is a decompression means for passing air between the oxygen-enriched membranes 23 to obtain air with a high oxygen concentration, and a blower means for supplying fresh air to the oxygen-enriched membranes 23 The fan 25 is configured.

そして、前記酸素富化装置20で生成した高濃度の酸素を追い焚き循環回路20に供給する混入手段27が追い焚き循環回路20に取り付けられており、酸素富化装置20で生成された高濃度の酸素は真空ポンプ24の駆動に連動して追い焚き循環回路20を流れる循環水中に混入される。この混入手段27の構成としては、例えばエゼクタのような循環水に対する絞りを設けて酸素富化装置26からの酸素を引っ張る構成を用いることで、流れに負圧を発生させて酸素富化空気を混入させれば多量の酸素を入れることができ、効果が大きい。ここで、加熱された後の循環水に酸素富化空気を混入する構成とした点に特徴があり、加熱される以前に混入すると、熱交換器12を通過中に異常音が発生したり、熱交換器12の腐食を促進したりする恐れがあるからである。   And the mixing means 27 which supplies the high concentration oxygen produced | generated by the said oxygen enricher 20 to the recirculation circuit 20 is attached to the recirculation circuit 20, and the high concentration produced | generated by the oxygen enricher 20 is provided. The oxygen is mixed into the circulating water flowing through the recirculation circuit 20 in conjunction with the driving of the vacuum pump 24. As the configuration of the mixing means 27, for example, a configuration is used in which a throttle for circulating water such as an ejector is provided to pull oxygen from the oxygen enricher 26, thereby generating a negative pressure in the flow to generate oxygen-enriched air. If mixed, a large amount of oxygen can be added, and the effect is great. Here, it is characterized in that oxygen-enriched air is mixed into the circulating water after being heated, and if mixed before being heated, abnormal noise occurs while passing through the heat exchanger 12, This is because corrosion of the heat exchanger 12 may be accelerated.

また、浴槽21には通常の追い焚き動作時に循環される浴槽水を吐出する追焚きアダプタ22が設けられており、この追い焚きアダプター22より循環水と共に吐出することで浴槽全体に高濃度の酸素を泡状に噴出することができ、泡風呂感覚を満喫することができるとともに浴室内の酸素濃度を最適な状態に維持することができる。   Further, the bathtub 21 is provided with a reheating adapter 22 that discharges the bathtub water that is circulated during a normal reheating operation. By discharging with the circulating water from the reheating adapter 22, high concentration oxygen is added to the entire bathtub. Can be ejected in the form of bubbles, and the bubble bath sensation can be fully enjoyed and the oxygen concentration in the bathroom can be maintained in an optimum state.

このような基本的な富化酸素供給構成に加え、本実施形態では酸素富化膜23と真空ポンプ24の間の酸素供給経路に第1の空気切替弁29を配設し、真空ポンプ24と混入手段27の間の酸素供給経路に第2の空気切替弁30を配設してある。この第1の空気切替弁29及び第2の空気切替弁30は共に一方が大気開放状態となるように切り替えが可能な三方弁で構成しており、第1の空気切替弁29及び第2の空気切替弁30を共に大気開放側に切り替えて真空ポンプ24を駆動させると、第1の空気切替弁29から大気を吸い込み第2の空気切替弁30から大気に排出する、いわゆるパージ運転をすることができ、酸素供給経路内に残留している結露水等の排出動作が可能となる。   In addition to such a basic enriched oxygen supply configuration, in this embodiment, a first air switching valve 29 is provided in the oxygen supply path between the oxygen enriched film 23 and the vacuum pump 24, A second air switching valve 30 is disposed in the oxygen supply path between the mixing means 27. Both the first air switching valve 29 and the second air switching valve 30 are configured as three-way valves that can be switched so that one of them is open to the atmosphere, and the first air switching valve 29 and the second air switching valve 29 When both the air switching valve 30 are switched to the atmosphere open side and the vacuum pump 24 is driven, a so-called purge operation is performed in which the atmosphere is sucked from the first air switching valve 29 and discharged from the second air switching valve 30 to the atmosphere. This makes it possible to discharge condensed water remaining in the oxygen supply path.

また、第1の空気切替弁29を大気開放側に切り替え、第2の空気切替弁30を酸素供給経路側に切り替えて真空ポンプ24を駆動させると、一般的な空気混入運転も可能となり、色々な運転形態を提供することができる。   Further, when the first air switching valve 29 is switched to the atmosphere opening side, the second air switching valve 30 is switched to the oxygen supply path side and the vacuum pump 24 is driven, a general air mixing operation becomes possible. Can be provided.

以上のように構成された酸素富化給湯装置において、図示しない操作部により運転指示が出され、給湯運転の場合はカラン17が操作されると、所定のシーケンスに基づいてバーナ10の燃焼が開始され所定温度の湯が出湯される。次ぎに、風呂追い焚き運転の指示が出された場合は、同様にバーナ10の燃焼が開始され風呂ポンプ18が駆動することで浴槽水が追い焚き循環回路20を循環し熱交換器12で加熱され浴槽内湯温を昇温して追い焚き動作を行う。   In the oxygen-enriched hot water supply apparatus configured as described above, when an operation instruction is issued by an operation unit (not shown) and the currant 17 is operated in the case of a hot water supply operation, combustion of the burner 10 starts based on a predetermined sequence. Then, hot water of a predetermined temperature is discharged. Next, when a bath rebirth operation instruction is issued, the combustion of the burner 10 is similarly started and the bath pump 18 is driven so that the bath water circulates through the recirculation circuit 20 and is heated by the heat exchanger 12. The temperature of the hot water in the bathtub is raised to perform a chasing operation.

そして、酸素混入運転が指示されると、上記風呂追い焚き運転の場合と同様に、風呂ポンプ18により浴槽水が追い焚き循環回路20を循環する。この時、送風ファン25も駆動されるため大気の吸い込み動作が開始され、この多量に吸い込まれた新鮮空気は酸素富化膜23に供給される。この新鮮空気が酸素富化膜23を通過するとき、真空ポンプ23が動作することで通過空気を減圧して酸素のみを取り出し、高濃度酸素として酸素供給経路より混入手段27に供給する。混入手段27では追い焚き循環回路20を流れる循環水により作用するエジェクタ効果で前記酸素供給経路より供給される高濃度酸素を吸い込み循環水に混入する。混入した酸素は追い焚きアダプタ22より浴槽内に噴出される。   When the oxygen mixing operation is instructed, the bath water is circulated through the recirculation circuit 20 by the bath pump 18 as in the case of the reheating operation. At this time, since the blower fan 25 is also driven, an air suction operation is started, and the fresh air sucked in a large amount is supplied to the oxygen-enriched film 23. When this fresh air passes through the oxygen-enriched film 23, the vacuum pump 23 operates to depressurize the passing air and take out only oxygen, and supply it as high-concentration oxygen to the mixing means 27 from the oxygen supply path. In the mixing means 27, high concentration oxygen supplied from the oxygen supply path is sucked and mixed into the circulating water by an ejector effect which is acted on by the circulating water flowing in the recirculation circuit 20. The mixed oxygen is ejected from the reheating adapter 22 into the bathtub.

この酸素混入運転において長時間連続して運転が継続されると、送風ファン25より取り込まれる新鮮空気中に水蒸気や湿気の多い空気が含まれている場合、酸素富化膜23で酸素を取り出すとき空気中の水分も同時に取り込んでしまい、酸素供給経路内に結露水として残留することになり、この残留結露水が雑菌の繁殖や低温時における凍結の原因となって、正常な酸素混入運転を阻害することになる。   When the operation is continued continuously for a long time in this oxygen-mixing operation, when the fresh air taken in from the blower fan 25 contains water vapor or moisture, the oxygen-enriched film 23 takes out oxygen. Moisture in the air is taken in at the same time and remains in the oxygen supply path as condensed water. This residual condensed water causes the growth of various bacteria and freezes at low temperatures, impeding normal oxygen mixing operation. Will do.

そこで本実施形態では、上記した如く、酸素富化膜23と真空ポンプ24の間の酸素供給経路に第1の空気切替弁29を配設し、真空ポンプ24と混入手段27の間の酸素供給経路に第2の空気切替弁30を配設してある。そして、酸素混入運転を終了した後に、前記第1の空気切替弁29及び第2の空気切替弁30を共に大気開放状態で連通するように切り替え、真空ポンプ24を所定時間駆動させる。この動作により、例えば酸素混入運転中に酸素供給経路内に結露水が残留していたとしても、酸素供給経路内を大気開放状態で新鮮空気を流通させるパージ運転により、結露水を大気に排出、乾燥させることができるものである。   Therefore, in the present embodiment, as described above, the first air switching valve 29 is disposed in the oxygen supply path between the oxygen-enriched film 23 and the vacuum pump 24, and the oxygen supply between the vacuum pump 24 and the mixing means 27 is performed. A second air switching valve 30 is disposed in the path. Then, after the oxygen mixing operation is finished, both the first air switching valve 29 and the second air switching valve 30 are switched so as to communicate with each other in an open state, and the vacuum pump 24 is driven for a predetermined time. By this operation, for example, even if dew condensation water remains in the oxygen supply path during the oxygen mixing operation, the dew condensation water is discharged to the atmosphere by the purge operation in which fresh air is circulated in the oxygen supply path in an open state. It can be dried.

さらに、上記第1の空気切替弁29と第2の空気切替弁30を大気開放状態で連通するように切り替え、真空ポンプ24を所定時間駆動させる場合は、送風ファン25を停止状態とし、酸素富化膜23に新鮮空気を供給しない状態、つまり酸素富化膜23から水蒸気等の湿気を含む空気を吸い込むことなく、パージ動作を行うことにより酸素供給経路内の残留結露水を確実に排出、乾燥するようにしている。   Further, when the first air switching valve 29 and the second air switching valve 30 are switched so as to communicate with each other in an air-released state and the vacuum pump 24 is driven for a predetermined time, the blower fan 25 is stopped and oxygen rich In a state in which fresh air is not supplied to the chemical film 23, that is, without purging air containing moisture such as water vapor from the oxygen-enriched film 23, residual condensed water in the oxygen supply path is reliably discharged and dried by performing a purge operation. Like to do.

また、図2に示すように、酸素混入運転を開始して一定時間Aが経過したことを検知した場合、一定時間Bの間は送風ファン25を停止した状態で真空ポンプ24を動作させるシーケンスを組み込む事により、酸素配管内には乾燥空気が流れることになり、ユーザーが浴槽アダプタからの気泡を楽しみつつ、配管内の結露水を排出、乾燥することが出来る。また、常に配管内の結露水の残留量を一定値以内に保つことが出来る。   In addition, as shown in FIG. 2, when it is detected that a certain time A has elapsed since the start of the oxygen mixing operation, a sequence for operating the vacuum pump 24 with the blower fan 25 stopped for a certain time B is performed. By incorporating it, dry air flows in the oxygen pipe, and the user can discharge and dry the condensed water in the pipe while enjoying air bubbles from the bathtub adapter. Moreover, the residual amount of dew condensation water in the pipe can always be kept within a certain value.

以上のように本発明の酸素富化給湯装置は、酸素混入運転を連続で長時間続けた場合に生じる水蒸気の吸い込みによる酸素供給経路の配管内に結露水が残留する現象を前記酸素富化膜と減圧手段の間及び減圧手段と混入手段との間に配設した空気切替弁を制御することで、酸素供給経路が大気開放経路となるようにし、配管内に残留した結露水を排出、乾燥させることができるため、追焚き循環回路を有する給湯器の追焚き配管を利用して、浴槽内の浴水中に酸素を供給する24時間風呂等にも適用することができる。   As described above, the oxygen-enriched hot water supply apparatus of the present invention exhibits the phenomenon in which condensed water remains in the piping of the oxygen supply path due to the suction of water vapor that occurs when the oxygen-mixing operation is continuously continued for a long time. By controlling the air switching valve disposed between the pressure reducing means and between the pressure reducing means and the mixing means, the oxygen supply path becomes an air release path, and the condensed water remaining in the pipe is discharged and dried. Therefore, the present invention can be applied to a 24-hour bath for supplying oxygen into bath water in a bathtub by using a reheating pipe of a water heater having a recirculation circuit.

本発明の実施の形態1における酸素富化給湯装置の全体構成図Overall configuration diagram of oxygen-enriched hot water supply apparatus according to Embodiment 1 of the present invention 同給湯装置における連続運転時のタイムチャートTime chart for continuous operation in the hot water supply system 従来の酸素富化装置の構成図Configuration diagram of conventional oxygen enricher

符号の説明Explanation of symbols

18 ポンプ
20 追焚き循環回路
21 浴槽
22 追焚きアダプタ
23 酸素富化膜
24 真空ポンプ(減圧手段)
26 酸素富化装置
27 混入手段
29 第1の空気切替弁
30 第2の空気切替弁
18 Pump 20 Recirculation circuit 21 Bath 22 Reheating adapter 23 Oxygen-enriched membrane 24 Vacuum pump (pressure reduction means)
26 Oxygen enrichment device 27 Mixing means 29 First air switching valve 30 Second air switching valve

Claims (6)

循環ポンプにより浴槽の湯を循環する追い焚き循環回路と、前記浴槽に設けた追い焚きアダプタと、減圧手段により酸素富化膜に空気を通過させることにより高濃度の酸素を取出す酸素富化装置と、前記酸素富化装置からの高濃度の酸素を追い焚き循環回路に混入させる混入手段とを有し、前記追焚きアダプタの噴出口より循環水に混入させた高濃度の酸素を噴出させる構成としたものであって、前記酸素富化膜と減圧手段の間及び減圧手段と混入手段との間に大気開放経路が形成可能となる空気切り替え弁を備えた酸素富化給湯装置。 A recirculation circuit that circulates hot water in the bathtub by a circulation pump, a reheating adapter provided in the bathtub, and an oxygen enricher that takes out high-concentration oxygen by allowing air to pass through the oxygen-enriched membrane by a decompression means; And a mixing means for mixing high-concentration oxygen from the oxygen-enriching device into the recirculation circuit, and a structure for ejecting high-concentration oxygen mixed into the circulating water from the spout of the reheating adapter; An oxygen-enriched hot water supply apparatus comprising an air switching valve capable of forming an air release path between the oxygen-enriched film and the depressurizing means and between the depressurizing means and the mixing means. 高濃度の酸素を追焚き循環回路に混入させた酸素混入運転を終了した場合、空気切り替え弁を所定時間大気開放側に切り替え、減圧手段を作動させて酸素供給経路に大気を流通させるようにした請求項1記載の酸素富化給湯装置。 When the oxygen mixing operation in which high-concentration oxygen was chased and mixed in the circulation circuit was completed, the air switching valve was switched to the atmosphere opening side for a predetermined time, and the pressure reducing means was operated to circulate the atmosphere through the oxygen supply path. The oxygen-enriched hot water supply apparatus according to claim 1. 酸素富化膜に新鮮空気を供給するための送風手段を備えた請求項1または2記載の酸素富化給湯装置。 The oxygen-enriched hot water supply apparatus according to claim 1 or 2, further comprising a blowing means for supplying fresh air to the oxygen-enriched film. 高濃度の酸素を追焚き循環回路に混入させた酸素混入運転を終了した場合、送風手段を所定時間停止させ、酸素富化膜に空気を供給しない状態で減圧手段を作動させるようにした請求項1〜3のいずれか1項記載の酸素富化給湯装置。 Claims: When the oxygen mixing operation in which high-concentration oxygen is added and mixed in the circulation circuit is terminated, the blowing means is stopped for a predetermined time, and the pressure reducing means is operated without supplying air to the oxygen-enriched membrane. The oxygen-enriched hot water supply device according to any one of 1 to 3. 高濃度の酸素を追焚き循環回路に混入させた酸素混入運転を終了した場合、送風手段を所定時間停止させ、減圧手段と混入手段の間に設けた空気切り替え弁を大気開放側に切り替えた状態で減圧手段を作動させるようにした請求項1または3記載の酸素富化給湯装置。 When the oxygen mixing operation in which high-concentration oxygen is added and mixed in the circulation circuit is terminated, the air blowing means is stopped for a predetermined time, and the air switching valve provided between the pressure reducing means and the mixing means is switched to the atmosphere opening side. The oxygen-enriched hot water supply apparatus according to claim 1 or 3, wherein the decompression means is operated. 高濃度の酸素を追焚き循環回路に混入させた酸素混入運転中に予め設定した所定時間を検知した場合、送風手段を所定時間停止させ、酸素富化膜に空気を供給しない状態で減圧手段を作動させるようにした請求項1または3記載の酸素富化給湯装置。 When a predetermined time is detected during the oxygen mixing operation in which high-concentration oxygen is added and mixed in the circulation circuit, the blowing means is stopped for a predetermined time, and the pressure reducing means is not supplied to the oxygen-enriched membrane. The oxygen-enriched hot water supply apparatus according to claim 1 or 3, wherein the apparatus is operated.
JP2003348205A 2003-10-07 2003-10-07 Oxygen enriched hot water supply device Pending JP2005110913A (en)

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