JP2010117073A - Bath water dirt decomposition device and water heater with reheating function including the same - Google Patents

Bath water dirt decomposition device and water heater with reheating function including the same Download PDF

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JP2010117073A
JP2010117073A JP2008290352A JP2008290352A JP2010117073A JP 2010117073 A JP2010117073 A JP 2010117073A JP 2008290352 A JP2008290352 A JP 2008290352A JP 2008290352 A JP2008290352 A JP 2008290352A JP 2010117073 A JP2010117073 A JP 2010117073A
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electrode
dirt
bath water
hot water
pipe
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JP5264428B2 (en
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Shoji Miyashita
章志 宮下
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Mitsubishi Electric Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To obtain a bath water dirt decomposition device easily maintaining clean bath water. <P>SOLUTION: The bath water dirt decomposition device 100 is constituted by using a positive electrode and a negative electrode arranged within piping (return pipe 70b) for reheating in a water heater 130 with a reheating function for taking out the bath water 150a from a bathtub 150, heating the bath water 150a and then, returning it to the bathtub 150 and a power source 91 for applying voltage to the positive electrode and negative electrode. By discharge generated between the positive electrode and negative electrode by applying predetermined voltage from the power source 91 to the positive electrode and negative electrode, dirt in the bath water 150a is decomposed. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、浴水に含まれる汚れや浴槽に接続された配管等に付着した汚れを分解することができる浴水汚れ分解装置、およびこれを備えた追焚き機能付き給湯機に関する。   The present invention relates to a bath water dirt decomposing apparatus capable of decomposing dirt contained in bath water and dirt attached to piping connected to a bathtub, and a hot water supply device with a chasing function provided with the same.

貯湯タンクに貯留した湯を熱源として用いる熱交換器により浴槽の浴水を追焚き可能な追焚き機能付き給湯機では、人体から浴水に洗い落とされた皮脂、角質等の汚れ成分が浴槽から追焚き用の往き管、追焚き用の熱交換器、追焚き用の戻り管を経て再び浴槽へと循環する。このため、追焚き用の配管(往き管、戻り管)の内面や追焚き用の熱交換器の内面、浴槽の内面には、上記の汚れ成分が不可避的に付着し、堆積する。そして、配管の内面や熱交換器の内面での汚れ成分の付着量がある程度多くなると、追焚き時に当該汚れ成分が浴槽へと流れ出て浴槽内の浴水を汚したり、ロドトルーラ属の細菌等が繁殖してぬめり感のある表面堆積物を形成したりする。また、追焚き用の熱交換器の内面の汚れは、熱交換効率を低下させる。   In a water heater with a reheating function that can recharge bath water in a bathtub with a heat exchanger that uses hot water stored in a hot water storage tank as a heat source, dirt components such as sebum and keratin that have been washed away from the human body by the bath water are removed from the bathtub. It circulates again to the bathtub through the return pipe for tracking, the heat exchanger for tracking, and the return pipe for tracking. For this reason, the above-mentioned dirt component inevitably adheres to and accumulates on the inner surface of the reheating pipe (forward pipe, return pipe), the inner surface of the reheating heat exchanger, and the inner surface of the bathtub. If the amount of dirt components attached to the inner surface of the pipe or the heat exchanger increases to a certain extent, the dirt components flow out into the bathtub when chasing and pollute the bath water in the bathtub, or Rhodotorula bacteria etc. It breeds to form slimy surface deposits. In addition, dirt on the inner surface of the heat exchanger for chasing reduces the heat exchange efficiency.

上記配管の内面や熱交換器の内面に付着し、堆積した汚れ成分や該汚れ成分中で繁殖した細菌は、市販の発泡性洗浄剤を用いて洗浄除去することができるが、環境への負荷を考慮すると洗浄剤をできるだけ用いずに汚れ成分や細菌を除去することが好ましく、工業分野では微小泡により汚れを除去する洗浄装置も開発されている。例えば特許文献1には、洗浄水を収容する洗浄槽と、洗浄槽中に被洗浄物を載置するハンガーと、洗浄水と気体とを混合して多数の微小気泡を含んだ流れを発生させ、該流れを被洗浄物に射出するインゼクターとを具備した洗浄装置が記載されている。この洗浄装置では、洗浄により被洗浄物から分離した汚れ(油脂)をオーバーフロー槽に溜め、汚れを分離した後のきれいな水を洗浄槽に再び戻すオーバーフロー系が必要に応じて設けられる。   The dirt components deposited on the inner surface of the pipe and the inner surface of the heat exchanger, and the bacteria that have propagated in the soil components, can be washed away using a commercially available foaming detergent, Therefore, it is preferable to remove dirt components and bacteria without using a cleaning agent as much as possible, and in the industrial field, a cleaning apparatus for removing dirt by microbubbles has been developed. For example, in Patent Document 1, a washing tank containing washing water, a hanger for placing an object to be washed in the washing tank, and washing water and gas are mixed to generate a flow containing a large number of microbubbles. And a cleaning device including an injector for injecting the flow onto an object to be cleaned. In this cleaning apparatus, an overflow system is provided as needed to accumulate dirt (oils and fats) separated from an object to be cleaned by washing in an overflow tank and return clean water after separating the dirt back to the washing tank.

特開2007−136275号公報JP 2007-136275 A

浴水中の汚れ成分や細菌(以下、「汚れ」と総称する)を除去するにあたって特許文献1に記載された方法を適用すると、汚れが浮遊した浴水をオーバーフローさせることになり、湯の節約という観点から望ましくなくなる。勿論、オーバーフローさせた浴水をオーバーフロー槽に溜め、汚れを分離した後のきれいな浴水を浴槽に再び戻すオーバーフロー系を設ければ湯の節約につながるが、このようなオーバーフロー系を浴槽に設けることは困難である。また、追焚き用の配管の内面や熱交換器の内面を清浄に保つにあたっては、これらの清浄化に伴って汚れが浴槽内に流入して入浴者の身体に再付着してしまうのを防止することが望まれる。   When the method described in Patent Document 1 is applied to remove dirt components and bacteria (hereinafter collectively referred to as “dirt”) in the bath water, the bath water in which the dirt floats will overflow, which saves hot water. Undesirable from the point of view. Of course, if you provide an overflow system that stores overflowed bath water in the overflow tank and returns the clean bath water after separating dirt back to the bathtub, it will lead to savings in hot water. It is difficult. In addition, when keeping the inner surface of the piping for reheating and the inner surface of the heat exchanger clean, dirt is prevented from flowing into the bathtub and reattaching to the body of the bather. It is desirable to do.

本発明は上記の事情に鑑みてなされたものであり、浴水の清浄化を図り易い簡便な浴水汚れ分解装置およびこれを備えた貯湯式給湯機を得ることを目的とする。   The present invention has been made in view of the above circumstances, and an object of the present invention is to obtain a simple bath water stain decomposing apparatus that facilitates cleaning of bath water and a hot water storage type water heater provided with the same.

本発明の浴水汚れ分解装置は、浴槽から浴水を取り出して加熱した後に浴槽に戻す追焚き機能付き給湯機での追焚き用の配管に取り付けられる浴水汚れ分解装置であって、追焚き用の配管内に配置されるプラス電極およびマイナス電極と、プラス電極とマイナス電極とに電圧を印加して、プラス電極とマイナス電極との間に放電を生じさせる電源部とを備え、追焚き用の配管を流れる浴水中の汚れを放電により分解するものである。   The bath water dirt decomposing apparatus of the present invention is a bath water dirt decomposing apparatus that is attached to a pipe for reheating in a hot water heater with a reheating function that takes out the bath water from the bathtub and heats it and then returns it to the bathtub. A plus electrode and a minus electrode arranged in the pipe for use, and a power supply unit that applies a voltage to the plus electrode and the minus electrode to generate a discharge between the plus electrode and the minus electrode. The dirt in the bath water flowing through the pipe is decomposed by electric discharge.

本発明の浴水汚れ分解装置は、浴槽から追焚き用の往き管、追焚き用の熱交換器、追焚き用の戻り管を経て再び浴槽へと循環する浴水中の汚れ成分や細菌を放電により無害で極微小な有機物に分解するものであるので、装置構成およびその使用が簡便であり、浴水の清浄化を容易に図ることができる。   The bath water dirt decomposing apparatus of the present invention discharges dirt components and bacteria in the bath water circulating again from the bathtub to the bathtub through the follow-up pipe for reheating, the heat exchanger for reheating, and the return pipe for reheating. Therefore, the apparatus configuration and its use are simple and the bath water can be easily cleaned.

以下、本発明の浴水汚れ分解装置および追焚き機能付き給湯機それぞれの実施の形態について、図面を参照して詳細に説明する。なお、本発明は以下に説明する実施の形態に限定されるものではない。   Hereinafter, embodiments of the bath water dirt decomposing apparatus and the water heater with a chase function according to the present invention will be described in detail with reference to the drawings. The present invention is not limited to the embodiments described below.

実施の形態1.
図1は、本発明の追焚き機能付き給湯機の一例を示す概略図である。同図に示す追焚き機能付き給湯機130は、市水等の低温水を熱源機で湯に沸き上げて所望箇所に給湯する機能と、浴槽150内の浴水150aを追焚きする機能とを有するものであり、当該追焚き機能付き給湯機130は、ヒートポンプユニット10とタンクユニット110と制御装置120とを備えている。以下、追焚き機能付き給湯機130の各構成要素について説明する。
Embodiment 1 FIG.
FIG. 1 is a schematic view showing an example of a hot water heater with a reheating function according to the present invention. The water heater 130 with a reheating function shown in the figure has a function of boiling low-temperature water such as city water into hot water with a heat source device and supplying hot water to a desired location, and a function of reheating the bath water 150a in the bathtub 150. The hot water supply device 130 with the chasing function includes a heat pump unit 10, a tank unit 110, and a control device 120. Hereinafter, each component of the hot water heater 130 with a chasing function will be described.

上記のヒートポンプユニット10は、冷媒を圧縮する圧縮機1と、沸上げ用熱交換器3と、膨張弁5と、蒸発器7と、これらを環状に接続する循環配管9とによって構成された冷凍サイクルシステムを有し、熱源機として機能する。上記の冷凍サイクルシステムでは、二酸化炭素等の冷媒が圧縮機1で圧縮されて高温、高圧となった後に沸上げ用熱交換器3で放熱し、膨張弁5で減圧され、蒸発器7で吸熱してガス状態となって圧縮機1に吸入される。冷媒として二酸化炭素を用いる場合、高圧側では該二酸化炭素の臨界圧を超える条件下で運転することが好ましい。この冷凍サイクルシステムは、ユニットケースUC1に納められている。 The heat pump unit 10 includes a compressor 1 that compresses refrigerant, a heat exchanger 3 for boiling, an expansion valve 5, an evaporator 7, and a refrigeration pipe 9 that connects these in an annular shape. It has a cycle system and functions as a heat source machine. In the above refrigeration cycle system, a refrigerant such as carbon dioxide is compressed by the compressor 1 to become high temperature and high pressure, and then radiates heat by the boiling heat exchanger 3, depressurizes by the expansion valve 5, and absorbs heat by the evaporator 7. As a result, it enters a gas state and is sucked into the compressor 1. When carbon dioxide is used as the refrigerant, it is preferable to operate on the high pressure side under conditions that exceed the critical pressure of the carbon dioxide. The refrigeration cycle system is housed in the unit case UC 1.

一方、タンクユニット110は、貯湯タンク20、給水管路30、貯湯用循環管路40、給湯管路50、一次側循環管路60、二次側循環管路70、追焚き用熱交換器80、および浴水汚れ分解装置100を有している。   On the other hand, the tank unit 110 includes a hot water storage tank 20, a water supply line 30, a hot water circulation line 40, a hot water supply line 50, a primary side circulation line 60, a secondary side circulation line 70, and a reheating heat exchanger 80. , And a bath water dirt decomposing apparatus 100.

上記の貯湯タンク20は、給水管路30から供給される低温水を貯留すると共にヒートポンプユニット10で沸き上げられた湯を貯留する積層式の貯湯タンクである。この貯湯タンク20の下部には、給水管路30が接続される水導入口20aと、貯湯用循環管路40の往き管40aが接続される水導出口20bとが設けられており、当該貯湯タンク20の上部には、貯湯用循環管路40の戻り管40bが接続される温水導入口20cと、給湯管路50が接続される温水導出口20dとが設けられている。貯湯タンク20は、常に満水状態に保たれる。   The hot water storage tank 20 is a stacked hot water storage tank that stores the low-temperature water supplied from the water supply pipe 30 and the hot water boiled by the heat pump unit 10. Below the hot water storage tank 20, a water inlet 20a to which the water supply pipe 30 is connected and a water outlet 20b to which the forward pipe 40a of the hot water circulation pipe 40 is connected are provided. In the upper part of the tank 20, a hot water inlet 20c to which the return pipe 40b of the hot water storage circulation line 40 is connected and a hot water outlet 20d to which the hot water supply pipe 50 is connected are provided. The hot water storage tank 20 is always kept full.

給水管路30は、市水等の低温水を貯湯タンク20、給湯管路50、および所定の給湯先に供給する管路であり、第1〜第3給水管部30a〜30cおよび減圧弁(図示せず)を有している。第1給水管部30aは水道等の水源(図示せず)と貯湯タンク20の水導入口20aとを繋ぎ、第2給水管部30bは第1給水管部30aから分岐して該第1給水管部30aと後述の混合弁45a,45bとを繋ぎ、第3給水管部30cは第1給水管部30aから分岐して該第1給水管部30aと所定の給湯先とを繋ぐ。図示の例では、給湯先の例として1つの給湯栓160が示されている。減圧弁は、第1給水管部30aでの第3給水管部30cの分岐箇所よりも上流側に設けられて、水源からの低温水の水圧を所定値に減じる。図1においては、第1給水管部30aでの低温水の流れ方向を実線の矢印で示している。   The water supply pipe 30 is a pipe that supplies low-temperature water such as city water to the hot water storage tank 20, the hot water supply pipe 50, and a predetermined hot water supply destination. The first to third water supply pipe sections 30a to 30c and the pressure reducing valve ( (Not shown). The first water supply pipe section 30a connects a water source (not shown) such as a water supply and the water introduction port 20a of the hot water storage tank 20, and the second water supply pipe section 30b is branched from the first water supply pipe section 30a. The pipe part 30a is connected to mixing valves 45a and 45b described later, and the third water supply pipe part 30c is branched from the first water supply pipe part 30a to connect the first water supply pipe part 30a and a predetermined hot water supply destination. In the illustrated example, one hot water tap 160 is shown as an example of a hot water supply destination. The pressure reducing valve is provided upstream of the branch point of the third water supply pipe part 30c in the first water supply pipe part 30a, and reduces the water pressure of the low-temperature water from the water source to a predetermined value. In FIG. 1, the flow direction of the low temperature water in the 1st water supply pipe part 30a is shown by the solid line arrow.

貯湯用循環管路40は、貯湯タンク20の水導出口20bからヒートポンプユニット10中の沸上げ用熱交換器3を経由して貯湯タンク20の温水導入口20cに達する管路であり、三方弁33と貯湯用送水ポンプ35とが設けられた往き管40aと、戻り管40bと、バイパス管40cとを有している。往き管40aは水導出口20bと沸上げ用熱交換器3とを繋ぎ、戻り管40bは沸上げ用熱交換器3と温水導入口20cとを繋ぐ。バイパス管40cは、往き管40aでの沸上げ用熱交換器3の上流側に設けられた三方弁33により往き管40aから分岐して、往き管40aと戻り管40bとを接続する。凍結防止運転時には、貯湯タンク20から往き管40aに流入した水がバイパス管40cを通って戻り管40bに流れる。沸上げ用熱交換器3により湯を沸上げる沸上げ運転および上記凍結防止運転を可能にするために、往き管40aでの三方弁33の上流側に貯湯用送水ポンプ35が設けられている。   The hot water storage circulation line 40 is a pipe that reaches the hot water inlet 20c of the hot water storage tank 20 from the water outlet 20b of the hot water storage tank 20 through the boiling heat exchanger 3 in the heat pump unit 10, and is a three-way valve. 33, a forward pipe 40a provided with a hot water storage water pump 35, a return pipe 40b, and a bypass pipe 40c. The forward pipe 40a connects the water outlet 20b and the boiling heat exchanger 3 and the return pipe 40b connects the boiling heat exchanger 3 and the hot water inlet 20c. The bypass pipe 40c branches from the forward pipe 40a by a three-way valve 33 provided on the upstream side of the boiling heat exchanger 3 in the forward pipe 40a, and connects the forward pipe 40a and the return pipe 40b. During the freeze prevention operation, water that has flowed from the hot water storage tank 20 into the forward pipe 40a flows through the bypass pipe 40c to the return pipe 40b. In order to enable a boiling operation for boiling hot water by the boiling heat exchanger 3 and the antifreezing operation, a hot water storage water feed pump 35 is provided upstream of the three-way valve 33 in the forward pipe 40a.

給湯管路50は、貯湯タンク20に貯留された湯と給水管路30からの低温水とを第1混合弁45aまたは第2混合弁45bで混合して所定温度の温湯を調製し、該温湯を浴槽150や所定の給湯先、図示の例では給湯栓160に供給する管路であり、上記第1混合弁45aおよび第2混合弁45bの他に第1〜第3給湯管部50a〜50cを有している。第1給湯管部50aは貯湯タンク20の温水導出口20dと第1、第2混合弁45a,45bとを繋ぎ、第2給湯管部50bは第1混合弁45aと二次側循環管路70での戻り管70bとを繋ぎ、第3給湯管部50cは第2混合弁45bと給湯栓160とを繋ぐ。図1においては、給湯栓160からの湯水の流出方向を破線の矢印で示している。   The hot water supply pipe 50 prepares hot water at a predetermined temperature by mixing the hot water stored in the hot water storage tank 20 and the low temperature water from the water supply pipe 30 with the first mixing valve 45a or the second mixing valve 45b. 1 to the third hot water supply pipe portions 50a to 50c in addition to the first mixing valve 45a and the second mixing valve 45b. have. The first hot water supply pipe section 50a connects the hot water outlet 20d of the hot water storage tank 20 to the first and second mixing valves 45a and 45b, and the second hot water supply pipe section 50b is connected to the first mixing valve 45a and the secondary side circulation conduit 70. The third hot water supply pipe portion 50c connects the second mixing valve 45b and the hot water tap 160. In FIG. 1, the outflow direction of the hot water from the hot water tap 160 is indicated by a dashed arrow.

一次側循環管路60は、貯湯タンク20の温水導出口20dから追焚き用熱交換器80を経由して貯湯タンク20の下部に達する管路であり、往き管60aと、一次側送水ポンプ55が設けられた戻り管60bとを有している。往き管60aは貯湯タンク20の温水導出口20dと追焚き用熱交換器80上部の温水導入口80aとを繋ぎ、戻り管60bは追焚き用熱交換器80下部の温水導出口80bと貯湯タンク20の下部とを繋ぐ。図示の例では、第1給湯管部50aでの貯湯タンク20側の所定の区間が、往き管60aでの貯湯タンク側の区間を兼ねている。   The primary-side circulation pipe 60 is a pipe that reaches the lower part of the hot water storage tank 20 from the hot water outlet 20d of the hot water storage tank 20 via the reheating heat exchanger 80, and includes the forward pipe 60a and the primary side water supply pump 55. And a return pipe 60b. The forward pipe 60a connects the hot water outlet 20d of the hot water tank 20 and the hot water inlet 80a above the reheating heat exchanger 80, and the return pipe 60b connects the hot water outlet 80b below the reheating heat exchanger 80 and the hot water tank. Connect the bottom of 20. In the illustrated example, a predetermined section on the hot water storage tank 20 side in the first hot water supply pipe section 50a also serves as a section on the hot water storage tank side in the forward pipe 60a.

二次側循環管路70は、浴槽150から追焚き用熱交換器80を経由して再び浴槽150に戻る管路であり、二次側送水ポンプ65が設けられた往き管70aと、戻り管70bとを有している。往き管70aは浴槽150と追焚き用熱交換器80下部の浴水導入口80cとを繋ぎ、戻り管70bは追焚き用熱交換器80上部の浴水導出口80dと浴槽150とを繋ぐ。   The secondary-side circulation pipeline 70 is a pipeline that returns from the bathtub 150 to the bathtub 150 via the reheating heat exchanger 80, and the return pipe 70a provided with the secondary-side water pump 65 and the return pipe 70b. The forward pipe 70 a connects the bathtub 150 and the bath water inlet 80 c below the reheating heat exchanger 80, and the return pipe 70 b connects the bath water outlet 80 d above the reheating heat exchanger 80 and the bathtub 150.

追焚き用熱交換器80は、一次側循環管路60を流れる湯と二次側循環管路70を流れる浴水150aとの間で熱交換を行って浴水150aを加熱するものであり、図示の例では、複数の伝熱プレートが当該追焚き用熱交換器80での高さ方向に積層されたプレート式の水−水熱交換器が用いられている。一次側循環管路60および二次側循環管路70の各々を接続することができるように、追焚き用熱交換器80の上部には上述した温水導入口80aと浴水導出口80dが、また下部には上述した温水導出口80bと浴水導入口80cが設けられている。これらの導入口80a,80cおよび導出口80b,80dを有する追焚き用熱交換器80では、追焚き運転時に上部が下部に比べて高温になるので、熱交換量を高め易いと共に貯湯タンク20に戻す温水の温度を低め易い。このため、追焚き用熱交換器80として熱交換能力が高いプレート式の熱交換器を用いることにより、貯湯タンク20内に相当量の熱量が蓄積された状態で追焚き運転を行ったときでも貯湯タンク20下部での貯留水を低温状態に保ち易くなる。   The reheating heat exchanger 80 heats the bath water 150a by performing heat exchange between the hot water flowing through the primary side circulation line 60 and the bath water 150a flowing through the secondary side circulation line 70, In the illustrated example, a plate-type water-water heat exchanger in which a plurality of heat transfer plates are stacked in the height direction of the heating heat exchanger 80 is used. In order to be able to connect each of the primary side circulation line 60 and the secondary side circulation line 70, the hot water inlet 80 a and the bath water outlet 80 d described above are provided above the reheating heat exchanger 80. Further, the above-described hot water outlet 80b and bath water inlet 80c are provided in the lower part. In the reheating heat exchanger 80 having the inlets 80a and 80c and the outlets 80b and 80d, the upper part becomes higher than the lower part during the reheating operation. It is easy to lower the temperature of the returning warm water. For this reason, by using a plate-type heat exchanger having a high heat exchange capacity as the reheating heat exchanger 80, even when a reheating operation is performed in a state where a considerable amount of heat is accumulated in the hot water storage tank 20. It becomes easy to keep the water stored in the lower part of the hot water storage tank 20 at a low temperature.

浴水汚れ分解装置100は、二次側循環管路70を流れる浴水150a中の汚れ成分や細菌を放電により無害で極微小な有機物に分解して浴水150aを清浄化する装置であり、本発明の浴水汚れ分解装置に含まれる。図示の浴水汚れ分解装置100は、戻り管70b内に配置されたプラス電極とマイナス電極(いずれも図示せず)とを有する汚れ分解部90Aと、該汚れ分解部90Aのプラス電極とマイナス電極とに電圧を印加して当該プラス電極とマイナス電極との間に放電を生じさせる電源部91と、該電源部91の出力動作を制御する電源制御部92とを備えている。また、往き管70aに取り付けられて該往き管70aを流れる浴水150a中に微小泡を生じさせるエジェクタ部93aと、該エジェクタ部93aに接続されたガス導入管93bと、該ガス導入管93bでのエジェクタ部93a側に設けられてガス導入管93bへの浴水150aの流入を防止する逆止弁93cと、ガス導入管93bでのガス導入口側に設けられてガス導入管93bへの空気の流入を制御する電磁弁93dとを有する微小泡発生部93も備えている。   The bath water dirt decomposing apparatus 100 is an apparatus that cleans the bath water 150a by decomposing the dirt components and bacteria in the bath water 150a flowing through the secondary circulation circuit 70 into harmless and extremely fine organic substances by discharge. It is included in the bath water dirt decomposing apparatus of the present invention. The illustrated bath water dirt decomposing apparatus 100 includes a dirt decomposing part 90A having a plus electrode and a minus electrode (both not shown) arranged in the return pipe 70b, and a plus electrode and a minus electrode of the dirt decomposing part 90A. And a power source control unit 92 for controlling the output operation of the power source unit 91. The power source unit 91 generates a discharge between the positive electrode and the negative electrode. Further, an ejector portion 93a that is attached to the forward tube 70a and generates micro bubbles in the bath water 150a flowing through the forward tube 70a, a gas introduction tube 93b connected to the ejector portion 93a, and the gas introduction tube 93b A check valve 93c provided on the ejector portion 93a side to prevent the bath water 150a from flowing into the gas introduction pipe 93b, and an air supplied to the gas introduction pipe 93b provided on the gas introduction port side of the gas introduction pipe 93b. There is also provided a microbubble generator 93 having an electromagnetic valve 93d for controlling the inflow of water.

タンクユニット110を構成する上述の構成部材のうち、給水管路30、貯湯用循環管路40、給湯管路50、および二次側循環管路70をそれぞれ除いた残りの構成部材は、ユニットケースUC2に納められている。給水管路30、貯湯用循環管路40、給湯管路50、および二次側循環管路70の各々は、その一部がユニットケースUC2の外部にまで延在している。 Of the above-described components constituting the tank unit 110, the remaining components excluding the water supply conduit 30, hot water storage circulation conduit 40, hot water supply conduit 50, and secondary side circulation conduit 70 are unit cases. It is stored in UC 2 . A part of each of the water supply pipe 30, the hot water storage circulation pipe 40, the hot water supply pipe 50, and the secondary side circulation pipe 70 extends to the outside of the unit case UC 2 .

制御装置120は、上記のユニットケースUC2内に配置された制御装置本体120aと、台所や浴室等に配置されて制御装置本体120aに有線接続または無線接続されたリモートコントローラ120bとを有している。制御装置本体120aは、ヒートポンプユニット10、三方弁33、貯湯用送水ポンプ35、第1混合弁45a、第2混合弁45b、一次側送水ポンプ55、二次側送水ポンプ65、電源制御部92、および電磁弁93dに接続され、当該制御装置本体120aの入力装置として機能するリモートコントローラ120からユーザが入力した情報や指令等に応じてこれらの動作を制御する。 The control device 120 includes a control device main body 120a disposed in the unit case UC 2 and a remote controller 120b disposed in a kitchen, a bathroom, or the like and wired or wirelessly connected to the control device main body 120a. Yes. The controller main body 120a includes a heat pump unit 10, a three-way valve 33, a hot water storage water pump 35, a first mixing valve 45a, a second mixing valve 45b, a primary side water pump 55, a secondary side water pump 65, a power control unit 92, These operations are controlled in accordance with information and commands input by the user from the remote controller 120 connected to the electromagnetic valve 93d and functioning as an input device of the control device main body 120a.

したがって、追焚き機能付き給湯機130は、リモートコントローラ120bからユーザが入力した上述の情報や指令等に基づいて動作する。例えば、リモートコントローラ120bからユーザが入力した沸上げ開始時刻になると、制御装置120による制御の下にヒートポンプユニット10および貯湯用循環ポンプ35が起動されて沸上げ運転が開始され、貯湯タンク20に設けられた温度センサ(図示せず)の検知結果から所定温度の湯が貯湯タンク20に所定量貯留されたと判断されるまで継続される。この間、貯湯タンク20下部の水導出口20bから貯湯用循環管路40に低温水が流入し、ヒートポンプユニット10で湯に沸き上げられて貯湯タンク20上部の温水導入口20cから該貯湯タンク20に戻される。   Therefore, the hot water heater 130 with a chasing function operates based on the above-described information, instructions, etc. input by the user from the remote controller 120b. For example, when the boiling start time input by the user from the remote controller 120b is reached, the heat pump unit 10 and the hot water circulation pump 35 are activated under the control of the control device 120, and the boiling operation is started. This is continued until it is determined from the detection result of the temperature sensor (not shown) that a predetermined amount of hot water is stored in the hot water storage tank 20. During this time, low-temperature water flows from the water outlet 20b at the lower part of the hot water storage tank 20 into the hot water circulation circuit 40, is heated to hot water by the heat pump unit 10, and is supplied to the hot water storage tank 20 from the hot water inlet 20c at the upper part of the hot water storage tank 20. Returned.

また、リモートコントローラ120bからユーザが追焚き運転の開始指令を入力すると、制御装置120による制御の下に一次側送水ポンプ55および二次側送水ポンプ65が起動されて追焚き運転が開始されると共に、浴水汚れ分解装置100が起動されて浴水150aの清浄化が開始される。この追焚き運転は、例えば戻り管70bに配置された温度センサ(図示せず)の検知結果から浴槽150内の浴水150aが所定温度にまで加熱されたと判断されるまで継続される。   When the user inputs a chasing operation start command from the remote controller 120b, the primary side water pump 55 and the secondary side water pump 65 are activated under the control of the control device 120, and the chasing operation is started. Then, the bath water dirt decomposing apparatus 100 is activated and cleaning of the bath water 150a is started. This chasing operation is continued until, for example, it is determined from the detection result of a temperature sensor (not shown) arranged in the return pipe 70b that the bath water 150a in the bathtub 150 is heated to a predetermined temperature.

追焚き運転が行われている間、貯湯タンク20上部の温水導出口20dから一次側循環管路60に湯が流入する一方で、浴槽150から二次側循環管路70に浴水150aが流入し、一次側循環管路60を流れる湯と二次側循環管路70を流れる浴水150aとの間で追焚き用熱交換器80により熱交換が行われて浴水150aが加熱される。また、微小泡発生部93が往き管70a中の浴水150aに多数の微小泡を生じさせ、これらの微小泡が二次側循環管路70を流れる過程で往き管70a内、追焚き用熱交換器80内、および戻り管70b内の汚れ成分や細菌を吸着し、該微小泡に吸着した汚れ成分や細菌が汚れ分解部90Aでの放電により無害で極微小な有機物に分解されて、浴水150aが清浄化される。以下、汚れ分解部90Aの構造および該汚れ分解部90Aによる汚れの分解について、図2および図3を参照して詳述する。   While the reheating operation is performed, hot water flows from the hot water outlet 20d at the upper part of the hot water storage tank 20 into the primary circulation line 60, while the bath water 150a flows from the bathtub 150 into the secondary circulation line 70. Then, heat is exchanged between the hot water flowing through the primary side circulation pipe 60 and the bath water 150a flowing through the secondary side circulation pipe 70 by the reheating heat exchanger 80 to heat the bath water 150a. Further, the microbubble generator 93 generates a large number of microbubbles in the bath water 150a in the forward pipe 70a, and the microbubbles are heated in the forward pipe 70a in the process of flowing through the secondary circulation circuit 70. The dirt components and bacteria in the exchanger 80 and the return pipe 70b are adsorbed, and the dirt components and bacteria adsorbed to the microbubbles are decomposed into harmless and extremely fine organic substances by the discharge in the dirt decomposing unit 90A. Water 150a is cleaned. Hereinafter, the structure of the dirt decomposing unit 90A and the decomposition of the dirt by the dirt decomposing unit 90A will be described in detail with reference to FIGS.

図2は、図1に示した追焚き機能付き給湯機を構成している浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。同図に示すように、汚れ分解部90Aは、平板状を呈するプラス電極83a(汚れ分解時にプラスの極性にされる電極を意味する。以下同じ。)とマイナス電極85a(汚れ分解時にプラスの極性にされる電極を意味する。以下同じ。)とが戻り管70bの管径方向に一定間隔で交互に配置された構造を有している。プラス電極83aおよびマイナス電極85aの各々はチタン製の電極であり、各プラス電極83aは浴水汚れ分解装置100の電源部91(図1参照)のプラス端子91aに、また各マイナス電極85aは電源部91のマイナス端子91bに接続されている。なお、図2においては、戻り管70bでの浴水150a(図1参照)の流れ方向を白抜きの矢印で示している。   FIG. 2 is a perspective view schematically showing a dirt decomposing unit in the bath water dirt decomposing apparatus constituting the hot water supply device with a chasing function shown in FIG. 1. As shown in the figure, the dirt decomposing portion 90A has a flat electrode positive electrode 83a (meaning an electrode having a positive polarity when decomposing dirt; the same applies hereinafter) and a negative electrode 85a (positive polarity when degrading dirt). And the same shall apply hereinafter)) are arranged alternately at regular intervals in the pipe radial direction of the return pipe 70b. Each of the plus electrode 83a and the minus electrode 85a is an electrode made of titanium, each plus electrode 83a is connected to the plus terminal 91a of the power source 91 (see FIG. 1) of the bath water dirt decomposing apparatus 100, and each minus electrode 85a is a power source. It is connected to the minus terminal 91b of the part 91. In FIG. 2, the flow direction of the bath water 150a (see FIG. 1) in the return pipe 70b is indicated by a white arrow.

一般に、微小泡はマイナスに帯電しており、プラスに帯電している汚れ成分や細菌を吸着する。このため、往き管70aに設けた微小泡発生部93により追焚き運転時に浴水150aに多数の微小泡を生じさせると、往き管70aの内面、追焚き用熱交換器80(図1参照)の内面、および戻り管70bの内面に付着し、堆積した汚れ成分(角質や皮脂等)、および該堆積した汚れ成分中で繁殖した細菌等の汚れが微小泡に吸着する。   Generally, microbubbles are negatively charged and adsorb dirt components and bacteria that are positively charged. For this reason, if a large number of micro bubbles are generated in the bath water 150a during the reheating operation by the micro bubble generating part 93 provided in the outward tube 70a, the inner surface of the outward tube 70a, the reheating heat exchanger 80 (see FIG. 1). The dirt components (keratin, sebum, etc.) that adhere to the inner surface of the return pipe 70b and the inner surface of the return pipe 70b and the bacteria that have propagated in the deposited dirt component adsorb to the microbubbles.

図3は、図2に示した汚れ分解部による汚れの分解を概略的に示す概念図である。同図に示すように、汚れGが吸着した微小泡MBは、浴水150aの流れに乗って汚れ分解部90Aに運ばれ、電源部91(図1参照)のプラス端子91a、マイナス端子91bから所定のパルス放電電圧を印加されたプラス電極83aとマイナス電極85aとの間に生じるパルス放電により、無害で極微小な有機物Orに分解される。このとき、プラス電極83aおよびマイナス電極85aそれぞれの表面およびその周囲は放電空間となる。パルス放電は、例えば追焚き運転の期間中、連続的に行われる。浴水150a中の汚れGを上記の放電によって有機物Orに分解する結果として、浴水150aが清浄化される。   FIG. 3 is a conceptual diagram schematically showing the decomposition of dirt by the dirt decomposition unit shown in FIG. As shown in the figure, the microbubbles MB adsorbed with the dirt G are carried to the dirt decomposing unit 90A along the flow of the bath water 150a, and from the plus terminal 91a and the minus terminal 91b of the power source unit 91 (see FIG. 1). By pulse discharge generated between the plus electrode 83a and the minus electrode 85a to which a predetermined pulse discharge voltage is applied, it is decomposed into harmless and extremely small organic matter Or. At this time, the surface of each of the positive electrode 83a and the negative electrode 85a and the periphery thereof is a discharge space. The pulse discharge is continuously performed, for example, during the follow-up operation. As a result of decomposing the dirt G in the bath water 150a into the organic substance Or by the above discharge, the bath water 150a is cleaned.

なお、図3においては、各プラス電極83aを実線で描いており、各マイナス電極85aを破線で描いている。また、プラス端子91aと各プラス電極83aとを接続する導線、およびマイナス端子91bと各マイナス電極85aとを接続する導線の各々を、便宜上、一点鎖線で描いている。そして、浴水150aにスマッジングを付すと共に該浴水150aの流れ方向を白抜きの矢印で示している。これらの点は、後述する実施の形態3〜9で参照する図5,6,8,9、11,12,14,15,17においても同様である。   In FIG. 3, each plus electrode 83a is drawn with a solid line, and each minus electrode 85a is drawn with a broken line. In addition, each of the conductive wire connecting the positive terminal 91a and each positive electrode 83a and the conductive wire connecting the negative terminal 91b and each negative electrode 85a is drawn with a one-dot chain line for convenience. The bathing water 150a is smudged and the flowing direction of the bathing water 150a is indicated by a white arrow. These points are the same in FIGS. 5, 6, 8, 9, 11, 12, 14, 15, and 17 referred to in Embodiments 3 to 9 described later.

上述した汚れ分解部90Aでのプラス電極83aとマイナス電極83bとの間隔を概ね5mm〜20mmの範囲内とし、電源部91から各電極83a,83bに印加するパルス放電電圧を概ね1kV〜30kVの範囲内にすると、上記の汚れGが無害で極微小な有機物Orに分解されることが確認された。汚れ分解部90Aによる汚れGの分解効果は、パルス放電電圧の周波数を100Hzから100kHzまで変化させても大きな違いはなかった。また、全ての電極83a,85aの極性をプラスに保って各電極83a,85aに微小泡MBを電気的に吸引し、個々の電極83a,85a表面での微小泡BMの密度を高めた後に電極85aの極性をマイナスに反転させて瞬間的にパルス放電を行っても、同様の汚れ分解効果を得ることができた。   The interval between the plus electrode 83a and the minus electrode 83b in the above-described dirt decomposition unit 90A is set within a range of about 5 mm to 20 mm, and the pulse discharge voltage applied from the power supply unit 91 to each of the electrodes 83a and 83b is set within a range of about 1 kV to 30 kV. It was confirmed that the soil G was decomposed into harmless and extremely fine organic matter Or. The effect of degrading the dirt G by the dirt decomposing unit 90A was not significantly different even when the frequency of the pulse discharge voltage was changed from 100 Hz to 100 kHz. Further, the polarities of all the electrodes 83a and 85a are kept positive, the micro bubbles MB are electrically attracted to the electrodes 83a and 85a, and the density of the micro bubbles BM on the surfaces of the individual electrodes 83a and 85a is increased. Even if the polarity of 85a is reversed to minus and the pulse discharge is performed instantaneously, the same dirt decomposition effect can be obtained.

上述のようにして汚れGを分解する浴水汚れ分解装置100(図1参照)は、装置構成およびその使用が簡便であり、当該浴水汚れ分解装置100を備えた追焚き機能付き給湯機130では、追焚き運転時に自動的に浴水150aが清浄化される。浴水150aの清浄化を容易に図ることができる。   The bath water dirt decomposing apparatus 100 (see FIG. 1) for decomposing the dirt G as described above is simple in apparatus configuration and use, and has a hot water supply device 130 with a chasing function provided with the bath water dirt decomposing apparatus 100. Then, the bath water 150a is automatically cleaned during the chasing operation. The bath water 150a can be easily cleaned.

実施の形態2.
図4は、本発明の他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。同図に示す汚れ分解部90Bは、円筒状を呈するプラス電極83bとマイナス電極85bとが一定間隔で同心円状に交互に配置された構造を有している。プラス電極83bおよびマイナス電極85bの各々はチタン薄板、タングステン薄板、ステンレス薄板、金属メッシュ等を円筒状に丸めたものであり、各プラス電極83bは浴水汚れ分解装置での電源部(図示せず)のプラス端子91aに、また各マイナス電極85bは上記電源部のマイナス端子91bに接続される。基材の表面にプラチナ、金、銀等をコーティングしたものをプラス電極83bとして用いると、放電による当該プラス電極83bの劣化が抑えられて電極寿命が大幅に延びる。図示を省略した浴水汚れ分解装置は、上述した汚れ分解部90Bの他に、プラス電極83bとマイナス電極85bとに電圧を印加して放電を生じさせる電源部と、該電源部の出力動作を制御する電源制御部とを備えている。
Embodiment 2. FIG.
FIG. 4 is a perspective view schematically showing a dirt decomposing portion in another bath water dirt decomposing apparatus of the present invention. The dirt decomposing portion 90B shown in the figure has a structure in which cylindrical positive electrodes 83b and negative electrodes 85b are alternately arranged in a concentric manner at regular intervals. Each of the plus electrode 83b and the minus electrode 85b is obtained by rolling a titanium thin plate, a tungsten thin plate, a stainless steel thin plate, a metal mesh or the like into a cylindrical shape, and each positive electrode 83b is a power supply unit (not shown) in a bath water dirt decomposing apparatus. ) And the minus electrodes 85b are connected to the minus terminal 91b of the power supply unit. When the surface of the base material coated with platinum, gold, silver or the like is used as the positive electrode 83b, the deterioration of the positive electrode 83b due to discharge is suppressed, and the electrode life is greatly extended. In addition to the above-described dirt decomposing unit 90B, the bath water dirt decomposing apparatus not shown in the figure performs a power supply unit that generates a discharge by applying a voltage to the positive electrode 83b and the negative electrode 85b, and an output operation of the power supply unit. And a power control unit for controlling.

図5は、図4に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。同図に示す例は、二次側循環回路の戻り管70bを途中の一定区間に亘って第1流路70b1と第2流路70b2とに分岐させた追焚き機能付き給湯機に図4の汚れ分解部90Bを配置した例であり、追焚き機能付き給湯機は、戻り管70bおよび汚れ分解部それぞれの構成を除き、図1に示した追焚き機能付き給湯機130と同様の構成を有している。 FIG. 5 is a conceptual diagram schematically showing an example of a usage pattern of the dirt decomposing unit shown in FIG. The example shown in the figure is a water heater with a reheating function in which a return pipe 70b of a secondary side circulation circuit is branched into a first flow path 70b 1 and a second flow path 70b 2 over a certain interval in the middle. 4 is an example in which the dirt decomposing unit 90B is arranged, and the hot water heater with a chasing function has the same configuration as the hot water heater with chasing function 130 shown in FIG. 1 except for the configuration of the return pipe 70b and the dirt decomposing unit. have.

上記第1流路70b1での浴槽側の端部は2つに分岐し、その一方は止水栓を兼ねた電極ホルダ部67aにより止水され、他方は第2流路70b2に合流している。第1流路70b1での上流側にモータMを有する電磁弁68aが設けられ、下流側にモータMを有する電磁弁68bが設けられ、これら2つの電磁弁68a,68bによって挟まれた区間に、汚れ分解部90Bの各電極83b,85bが電極ホルダ部67aにより保持されて配置されている。また、第2流路70b2には、モータMを有する電磁弁68cが設けられている。第1流路70b1と第2流路70b2とは、電磁弁68b,68cの下流側で互いに合流している。 The end portion on the bathtub side of the first flow path 70b 1 is branched into two, one of which is stopped by the electrode holder portion 67a which also serves as a water stop cock, and the other joins the second flow path 70b 2. ing. An electromagnetic valve 68a having a motor M is provided on the upstream side of the first flow path 70b 1 , and an electromagnetic valve 68b having a motor M is provided on the downstream side. In a section sandwiched between these two electromagnetic valves 68a and 68b, The electrodes 83b and 85b of the dirt decomposing portion 90B are held and arranged by the electrode holder portion 67a. The second flow path 70b 2 is provided with an electromagnetic valve 68c having a motor M. The first flow path 70b 1 and the second flow path 70b 2 merge with each other on the downstream side of the electromagnetic valves 68b and 68c.

追焚き運転時には、例えば追焚き機能付き給湯機の制御装置の制御の下に電磁弁68a,68bの各々が開弁されると共に電磁弁68cが閉弁される。浴水150aは、戻り管70bの第2流路70b2は流れずに第1流路70b1を流れて浴槽に戻る。図5中の上側の図に示すように、汚れGが吸着した微小泡MBは浴水150aの流れに乗って汚れ分解部90Bに運ばれる。そして、各プラス電極83bと各マイナス電極85bとに例えば10kVのパルス放電電圧を印加することでプラス電極83bとマイナス電極85bとの間に生じるパルス放電により、無害で極微小な有機物に分解される。パルス放電は、例えば追焚き運転の期間中、連続的に行われる。浴水150a中の汚れGを上記の有機物Orに分解する結果として、浴水150aが清浄化される。 During the chasing operation, for example, each of the solenoid valves 68a and 68b is opened and the solenoid valve 68c is closed under the control of the controller for the hot water heater with chasing function. The bath water 150a flows through the first flow path 70b 1 without flowing through the second flow path 70b 2 of the return pipe 70b and returns to the bathtub. As shown in the upper diagram in FIG. 5, the microbubbles MB on which the dirt G is adsorbed are carried on the flow of the bath water 150a and carried to the dirt decomposition unit 90B. Then, by applying a pulse discharge voltage of, for example, 10 kV to each plus electrode 83b and each minus electrode 85b, the pulse discharge generated between the plus electrode 83b and the minus electrode 85b is decomposed into harmless and extremely small organic substances. . The pulse discharge is continuously performed, for example, during the follow-up operation. As a result of decomposing the dirt G in the bath water 150a into the organic substance Or, the bath water 150a is cleaned.

放電現象により各電極83a,83bの表面が劣化して浴水汚れ分解装置の性能が低下し、各電極83b,85bの交換が必要になったときには、図5中の下側の図に示すように、例えば追焚き機能付き給湯機の制御装置の制御の下に電磁弁68a,68bの各々を閉弁させると共に電磁弁68cを開弁させて、浴水150aが第1流路70b1は流れずに第2流路70b2を流れるようにする。このように浴水150aの流路を切り替えると、追焚き運転中であっても電極ホルダ部67aを第1流路70b1から取り外すことで各電極83b,85bを戻り管70bから取り出すことができ、容易に交換することができる。勿論、各電極83b,85bを戻り管70bから取り出す際には、当該電極83b,85bへのパルス放電電圧の印加を中断しておく。 When the surface of each electrode 83a, 83b deteriorates due to the discharge phenomenon and the performance of the bath water dirt decomposing apparatus is lowered and the electrodes 83b, 85b need to be replaced, as shown in the lower diagram of FIG. to, for example, an electromagnetic valve 68a under the control of the control device of the reheating function water heaters, by opening the electromagnetic valve 68c along with to close the respective 68b, bath water 150a is the first passage 70b 1 flow to flow a second flow path 70b 2 without. By switching the flow path of the bath water 150a in this way, the electrodes 83b and 85b can be taken out from the return pipe 70b by removing the electrode holder portion 67a from the first flow path 70b 1 even during the chasing operation. Can be easily replaced. Of course, when the electrodes 83b and 85b are taken out from the return tube 70b, the application of the pulse discharge voltage to the electrodes 83b and 85b is interrupted.

図6は、図4に示した汚れ分解部の使用形態の他の例を概略的に示す概念図である。同図に示す例では、汚れ分解部の各電極への電圧の印加形態のみが図5に示した例とは異なり、まず、浴水150a中の汚れGを放電により分解する前に全ての電極83b,85bの極性をプラスにする。これにより、図6中の上側の図に示すように、汚れGが吸着した微小泡MBを各電極83b,85bに電気的に吸引して個々の電極83b,85b表面での微小泡BMの密度を高める。   FIG. 6 is a conceptual diagram schematically showing another example of the usage pattern of the dirt decomposing unit shown in FIG. In the example shown in the figure, only the voltage application form to each electrode of the soil decomposition unit is different from the example shown in FIG. 5. First, all the electrodes before the soil G in the bath water 150a is decomposed by electric discharge. The polarity of 83b and 85b is made positive. As a result, as shown in the upper diagram in FIG. 6, the microbubbles MB adsorbed with the dirt G are electrically attracted to the electrodes 83b and 85b, and the density of the microbubbles BM on the surfaces of the individual electrodes 83b and 85b. To increase.

この後、図6中の下側の図に示すように、浴水汚れ分解装置の電源部での端子91bの極性をマイナスに反転させて各プラス電極83bと各マイナス電極85bとにパルス放電電圧を印加する。これによりプラス電極83bとマイナス電極85bとの間にパルス放電が生じ、各電極83b,85bに電気的に吸引されていた微小泡MBに吸着している汚れGを無害で極微小な有機物に瞬間的に分解する。全ての電極83b,85bの極性をプラスにする動作とパルス放電動作とは、追焚き運転の期間中、交互に間欠的に行われる。このようにして汚れGを分解すると、パルス放電を連続的に行って汚れGを分解する場合に比べ、各電極83b,85bへのパルス放電電圧の総印加時間が短縮されるので、浴水汚れ分解装置のエネルギー消費量が低減され、ランニングコストが抑えられる。   Thereafter, as shown in the lower diagram in FIG. 6, the polarity of the terminal 91b in the power supply unit of the bath water dirt decomposing apparatus is inverted to minus, and the pulse discharge voltage is applied to each plus electrode 83b and each minus electrode 85b. Apply. As a result, a pulse discharge is generated between the plus electrode 83b and the minus electrode 85b, and the dirt G adsorbed on the microbubbles MB electrically attracted to the electrodes 83b and 85b is instantly turned into harmless and extremely fine organic matter. Disassemble. The operation of making all the electrodes 83b and 85b positive and the pulse discharge operation are alternately and intermittently performed during the follow-up operation. When the dirt G is decomposed in this way, the total application time of the pulse discharge voltage to the electrodes 83b and 85b is shortened as compared with the case where the dirt G is decomposed by continuously performing pulse discharge. The energy consumption of the decomposition apparatus is reduced, and the running cost is suppressed.

実施の形態3.
図7は、本発明の更に他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。同図に示す汚れ分解部90Cは、メッシュ状を呈するプラス電極83cとマイナス電極85cとが一定間隔で交互に配置された構造を有している。プラス電極83cおよびマイナス電極85cの各々は金属製のもの、またはセラミックスや合成樹脂により作製される基材の表面に吸着剤や酸化触媒等を添着させて導電性をも付与したものであり、各プラス電極83cは浴水汚れ分解装置での電源部(図示せず)のプラス端子91aに、また各マイナス電極85cは電源部のマイナス端子91bに接続される。図示を省略した浴水汚れ分解装置は、上述した汚れ分解部90Cの他に、プラス電極83cとマイナス電極85cとに電圧を印加して放電を生じさせる電源部と、該電源部の出力動作を制御する電源制御部とを備えている。
Embodiment 3 FIG.
FIG. 7 is a perspective view schematically showing a soil decomposing portion in still another bath water soil decomposing apparatus of the present invention. The dirt decomposing portion 90C shown in the figure has a structure in which positive electrodes 83c and negative electrodes 85c having a mesh shape are alternately arranged at regular intervals. Each of the plus electrode 83c and the minus electrode 85c is made of metal, or is provided with conductivity by attaching an adsorbent, an oxidation catalyst, or the like to the surface of a substrate made of ceramics or synthetic resin. The plus electrode 83c is connected to a plus terminal 91a of a power source (not shown) in the bath water dirt decomposing apparatus, and each minus electrode 85c is connected to a minus terminal 91b of the power source. In addition to the above-described soil decomposing unit 90C, the bath water soil decomposing device, which is not shown, has a power source unit that generates a discharge by applying a voltage to the positive electrode 83c and the negative electrode 85c, and an output operation of the power source unit. And a power control unit for controlling.

図8は、図7に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。同図に示す例は、二次側循環回路の戻り管70bを途中の一定区間に亘って第1流路70b1と第2流路70b2とに分岐させ、該第1流路70b1および第2流路70b2の各々を上流側の区間と下流側の区間とに分けて上流側の区間と下流側の区間とを継手を兼ねた電極ホルダ部67bで流路毎に接続した追焚き機能付き給湯機に図7の汚れ分解部90Cを2つ配置した例である。追焚き機能付き給湯機は、戻り管70bおよび汚れ分解部それぞれの構成を除き、図1に示した追焚き機能付き給湯機130と同様の構成を有している。 FIG. 8 is a conceptual diagram schematically showing an example of a usage pattern of the dirt decomposing unit shown in FIG. Example shown in the figure, is branched to the return pipe 70b of the secondary-side circulation circuit and the first passage 70b 1 over a predetermined section of the middle and the second flow path 70b 2, the first passage 70b 1 and Each of the second flow paths 70b 2 is divided into an upstream section and a downstream section, and the upstream section and the downstream section are connected to each flow path by the electrode holder portion 67b that also serves as a joint. It is an example which has arrange | positioned two dirt decomposition | disassembly parts 90C of FIG. The hot water heater with a chasing function has the same configuration as that of the hot water heater with chasing function shown in FIG. 1 except for the configurations of the return pipe 70b and the dirt decomposing unit.

上記第1流路70b1での上流側にはモータMを有する電磁弁68aが設けられ、下流側にはモータMを有する電磁弁68bが設けられ、これら2つの電磁弁68a,68bによって挟まれた区間に継手を兼ねた電極ホルダ部67bが設けられて、該電極ホルダ部67bにより汚れ分解部90Cの各電極83c,85cが保持されている。同様に、第2流路70b2での上流側にはモータMを有する電磁弁68cが設けられ、下流側にはモータMを有する電磁弁68dが設けられ、これら2つの電磁弁68c,68dによって挟まれた区間に継手を兼ねた電極ホルダ部67bが設けられて、該電極ホルダ部67bにより他の汚れ分解部90Cのプラス電極83cとマイナス電極85cとが保持されている。各汚れ分解部90Cでのプラス電極83cおよびマイナス電極85cの各々は、第1流路70b1または第2流路70b2での流路径方向に延在している。第1流路70b1と第2流路70b2とは、電磁弁68b,68dの下流側で互いに合流している。 The upstream side in the first passage 70b 1 solenoid valve 68a is provided with a motor M, the electromagnetic valve 68b is provided with a motor M on the downstream side, the two electromagnetic valves 68a, sandwiched between the 68b An electrode holder portion 67b that also serves as a joint is provided in the section, and the electrodes 83c and 85c of the soil decomposition portion 90C are held by the electrode holder portion 67b. Similarly, on the upstream side in the second flow path 70b 2 solenoid valve 68c is provided with a motor M, an electromagnetic valve 68d is provided with a motor M on the downstream side, the two electromagnetic valves 68c, by 68d An electrode holder portion 67b that also serves as a joint is provided in the sandwiched section, and the plus electrode 83c and the minus electrode 85c of the other soil decomposition portion 90C are held by the electrode holder portion 67b. Each of the plus electrode 83c and the minus electrode 85c in each dirt decomposition unit 90C extends in the flow path radial direction in the first flow path 70b 1 or the second flow path 70b 2 . The first flow path 70b 1 and the second flow path 70b 2 merge with each other on the downstream side of the electromagnetic valves 68b and 68d.

追焚き運転時には、例えば追焚き機能付き給湯機の制御装置の制御の下に電磁弁68a,68bの各々が閉弁されると共に電磁弁68c,68dの各々が開弁される。浴水150aは、戻り管70bの第1流路70b1は流れずに第2流路70b2を流れて浴槽に戻る。図8中の上側の図に示すように、汚れGが吸着した微小泡MBは浴水150aの流れに乗って第2流路70b2中の汚れ分解部90Cに運ばれ、各プラス電極83cと各マイナス電極85cとに例えば6kVのパルス放電電圧を印加することでプラス電極83cとマイナス電極85cとの間に生じるパルス放電により、無害で極微小な有機物に分解される。浴水150a中の汚れGを上記の有機物に分解する結果として、浴水150aが清浄化される。 During the chasing operation, for example, the solenoid valves 68a and 68b are closed and the solenoid valves 68c and 68d are opened under the control of the control device for the hot water heater with chasing function. Bath water 150a is the first passage 70b 1 of the return tube 70b is flows through the second flow path 70b 2 without flowing back to the tub. As shown in the upper diagram in FIG. 8, microbubbles MB dirt G is adsorbed is carried dirt decomposition portion 90C of the second flow path 70b in 2 on stream of bath water 150a, and each of the positive electrodes 83c By applying a pulse discharge voltage of 6 kV, for example, to each negative electrode 85c, the pulse discharge generated between the positive electrode 83c and the negative electrode 85c is decomposed into harmless and extremely small organic substances. As a result of decomposing the dirt G in the bath water 150a into the above organic substances, the bath water 150a is cleaned.

放電現象により各電極83c,85cの表面が劣化して浴水汚れ分解装置の性能が低下し、各電極83c,85cの交換が必要になったときには、図8中の下側の図に示すように、例えば追焚き機能付き給湯機の制御装置の制御の下に電磁弁68a,68bの各々を開弁させると共に電磁弁68c,68dの各々を閉弁させて、浴水150aが第2流路70b2は流れずに第1流路70b1を流れるようにする。このように浴水150aの流路を切り替えると、追焚き運転中であっても第2流路70b2中の電極ホルダ部67bを汚れ分解部90Cごと第2流路70b2から取り外すことで各電極83c,85cを戻り管70bから取り出すことができ、容易に交換することができる。 When the surface of each electrode 83c, 85c deteriorates due to the discharge phenomenon and the performance of the bath water dirt decomposing apparatus is lowered, and it is necessary to replace each electrode 83c, 85c, as shown in the lower diagram in FIG. For example, the solenoid valves 68a and 68b are opened and the solenoid valves 68c and 68d are closed under the control of the controller for the hot water heater with a reheating function. 70b 2 does not flow but flows through the first flow path 70b 1 . Thus switching the flow path of the bath water 150a, each by removing from the second flow path 70b 2 each decomposition unit 90C even reheating during operation dirt electrode holder portion 67b of the second flow path 70b in 2 The electrodes 83c and 85c can be taken out from the return pipe 70b and can be easily replaced.

実施の形態4.
図9は、図7に示した汚れ分解部の使用形態の他の例を概略的に示す概念図である。同図に示す例は、二次側循環回路の戻り管70bを途中の一定区間に亘って第1流路70b1と第2流路70b2とに分岐させ、第2流路70b2を上流側の区間と下流側の区間とに分けてこれらの区間を電極ホルダ部67bで接続すると共に、第2流路70b2の上流側に給湯管路中の第2給湯管部50bを接続し、第2流路70b2の下流側にドレイン管125を接続した追焚き機能付き給湯機に図7の汚れ分解部90Cを配置した例である。
Embodiment 4 FIG.
FIG. 9 is a conceptual diagram schematically showing another example of the usage pattern of the dirt decomposing unit shown in FIG. Example shown in the figure, is branched to the return pipe 70b of the secondary-side circulation circuit and the first passage 70b 1 over a predetermined section of the middle and the second flow path 70b 2, the second flow path 70b 2 upstream divided into the side of the section and the downstream section with connecting these sections in the electrode holder 67b, a second hot water pipe 50b of the hot water supply pipe path is connected to the upstream side of the second flow path 70b 2, an example in which the dirt decomposition section 90C of FIG. 7 in reheating function water heater is connected to the drain pipe 125 on the downstream side of the second flow path 70b 2.

この例での追焚き機能付き給湯機は、戻り管70bおよび汚れ分解部それぞれの構成、第2給湯管部50bと戻り管70bとの接続形態、およびドレイン管125の有無を除き、図1に示した追焚き機能付き給湯機130と同様の構成を有している。図示を省略した浴水汚れ分解装置は、上述した汚れ分解部90Cの他に、プラス電極83cとマイナス電極85cとに電圧を印加して放電を生じさせる電源部と、該電源部の出力動作を制御する電源制御部とを備えている。   The hot water supply device with a chasing function in this example is shown in FIG. 1 except for the configurations of the return pipe 70b and the dirt decomposing part, the connection form of the second hot water supply pipe part 50b and the return pipe 70b, and the presence or absence of the drain pipe 125. It has the same configuration as the hot water heater 130 with the chasing function shown. In addition to the above-described dirt decomposing unit 90C, the bath water stain decomposing apparatus, which is not shown, has a power supply unit that generates a discharge by applying a voltage to the positive electrode 83c and the negative electrode 85c, and an output operation of the power supply unit. And a power control unit for controlling.

上記第1流路70b1での上流側にはモータMを有する電磁弁68aが設けられ、下流側にはモータMを有する電磁弁68bが設けられている。また、第2流路70b2での第1流路70b1との分岐側にはモータMを有する電磁弁68cが設けられ、第1流路70b1との合流側にはモータMを有する電磁弁68dが設けられ、これら2つの電磁弁68c,68dによって挟まれた区間に継手を兼ねた電極ホルダ部67bが設けられて、該電極ホルダ部67bにより汚れ分解部90Cのプラス電極83cとマイナス電極85cとが保持されている。汚れ分解部90Cでの各電極83c,85cは、第2流路70b2での流路径方向に延在している。第1流路70b1と第2流路70b2とは、電磁弁68b,68dの下流側で互いに合流している。 Solenoid valve 68a is provided with a motor M on the upstream side in the first passage 70b 1, the electromagnetic valve 68b is provided with a motor M on the downstream side. In addition, an electromagnetic valve 68c having a motor M is provided on the second flow path 70b 2 where the first flow path 70b 1 is branched, and an electromagnetic valve 68c having a motor M is provided on the merge side with the first flow path 70b 1. A valve 68d is provided, and an electrode holder portion 67b that also serves as a joint is provided in a section sandwiched between the two electromagnetic valves 68c and 68d, and the electrode holder portion 67b allows the plus electrode 83c and the minus electrode of the dirt decomposition portion 90C. 85c is held. Each electrode 83c of the dirty decomposition unit 90C, 85c extend in a passage diameter direction of the second flow path 70b 2. The first flow path 70b 1 and the second flow path 70b 2 merge with each other on the downstream side of the electromagnetic valves 68b and 68d.

また、第2給湯管部50bは電磁弁68cの下流側で第2流路70b2に合流しており、当該第2給湯管部50bでの下流側にはモータMを有する電磁弁68eが設けられている。ドレイン管125は電磁弁68dの上流側で第2流路70b2から分岐しており、当該ドレイン管125での上流側にはモータMを有する電磁弁68fが設けられている。 The second hot water supply pipe section 50b is joined to the second flow path 70b 2 on the downstream side of the solenoid valve 68c, the electromagnetic valve 68e is provided with a motor M on the downstream side in the second supply pipe portion 50b It has been. The drain pipe 125 is branched from the second flow path 70b 2 on the upstream side of the electromagnetic valve 68d, and an electromagnetic valve 68f having a motor M is provided on the upstream side of the drain pipe 125.

追焚き運転時には、例えば追焚き機能付き給湯機の制御装置の制御の下に電磁弁68a,68b,68e、68fが閉弁されると共に電磁弁68c,68dの各々が開弁される。浴水150aは、戻り管70bの第1流路70b1は流れずに第2流路70b2を流れて浴槽に戻る。第2給湯管部50bから第2流路70b2への湯水の流入はない。また、浴水150a中の汚れGを放電により分解するのに先だって、浴水汚れ分解装置での電源部の各端子91a,91bの極性をプラスにすることで全ての電極83c,85cの極性をプラスにする。これにより、図9中の上側の図に示すように、汚れGが吸着した微小泡MBを各電極83c,85cに電気的に吸引して個々の電極83c,85c表面での微小泡BMの密度を高める。 During the chasing operation, for example, the solenoid valves 68a, 68b, 68e, and 68f are closed and the solenoid valves 68c and 68d are each opened under the control of the controller for the hot water heater with chasing function. The bath water 150a flows through the second flow path 70b 2 without flowing through the first flow path 70b 1 of the return pipe 70b and returns to the bathtub. No hot water flows from the second hot water supply pipe portion 50b to the second flow path 70b 2. In addition, before the dirt G in the bath water 150a is decomposed by electric discharge, the polarities of the terminals 91a and 91b of the power supply unit in the bath water dirt decomposing apparatus are made positive so that the polarities of all the electrodes 83c and 85c are changed. Make it plus. As a result, as shown in the upper diagram in FIG. 9, the microbubbles MB adsorbed with the dirt G are electrically attracted to the electrodes 83c and 85c, and the density of the microbubbles BM on the surfaces of the individual electrodes 83c and 85c. To increase.

この後、図9中の下側の図に示すように、例えば追焚き機能付き給湯機の制御装置の制御の下に電磁弁68a,68bの各々を開弁させると共に電磁弁68c,68dの各々を閉弁させて、浴水150aが第2流路70b2は流れずに第1流路70b1を流れて浴槽に戻るように流路を切り替える。また、電磁弁68e、68fの各々を開弁させて第2給湯管部50bからの湯水を第2流路70b2経由でドレイン管125に流す。さらには、電源部の端子91bの極性をマイナスに反転させて各プラス電極83cと各マイナス電極85cとにパルス放電電圧を印加する。これによりプラス電極83cとマイナス電極85cとの間にパルス放電が生じ、各電極83c,85cに電気的に吸引されていた微小泡MBに吸着している汚れGを無害で極微小な有機物に瞬間的に分解する。浴水150a中の汚れGを上記の有機物に分解する結果として、浴水150aが清浄化される。 Thereafter, as shown in the lower diagram in FIG. 9, for example, each of the solenoid valves 68a and 68b is opened and the solenoid valves 68c and 68d are respectively controlled under the control of the control device of the hot water heater with a reheating function. And the flow path is switched so that the bath water 150a flows through the first flow path 70b 1 and does not flow through the second flow path 70b 2 and returns to the bathtub. The electromagnetic valve 68e, flows into the drain pipe 125 in hot water the via second passage 70b 2 from the second hot water supply pipe portion 50b by opening the respective 68f. Further, the polarity of the terminal 91b of the power supply unit is inverted to minus and a pulse discharge voltage is applied to each plus electrode 83c and each minus electrode 85c. As a result, a pulse discharge is generated between the plus electrode 83c and the minus electrode 85c, and the dirt G adsorbed on the microbubbles MB electrically attracted to the electrodes 83c and 85c is instantly turned into harmless and extremely fine organic matter. Disassemble. As a result of decomposing the dirt G in the bath water 150a into the above organic substances, the bath water 150a is cleaned.

汚れGの分解により生じた無害で極微小な有機物は、第2給湯管部50bから第2流路70b2に供給される湯水の流れに乗ってドレイン管125に排出される。汚れ分解部90Cでの汚れGの分解により生じた上記の有機物が浴槽に流入してしまうことが防止されるので、浴水150aが更に清浄化される。図9の下側の図においては、第2給湯管部50bからの湯水の流れ方向を白抜きの破線の矢印で示してある。 Harmless very small organic materials produced by the decomposition of dirt G is discharged to the drain pipe 125 riding hot water flow supplied from the second hot water supply pipe portion 50b in the second flow path 70b 2. Since the organic matter generated by the decomposition of the dirt G in the dirt decomposition unit 90C is prevented from flowing into the bathtub, the bath water 150a is further cleaned. In the lower drawing of FIG. 9, the flowing direction of the hot water from the second hot water supply pipe section 50b is indicated by a white broken arrow.

なお、電磁弁68a,68bの各々が閉弁し、電磁弁68c,68d,68e,68fの各々が開弁した状態で全ての電極83c,85cの極性をマイナスにしたところ、個々の電極83c,85cに電気的に吸引されていた微小泡MBを各電極83c,85cから脱離させて、汚れGが吸着したままドレイン管125に排出することができた。   When the solenoid valves 68a and 68b are closed and the solenoid valves 68c, 68d, 68e and 68f are opened, the polarities of all the electrodes 83c and 85c are made negative. The microbubbles MB electrically attracted to 85c can be detached from the electrodes 83c and 85c and discharged to the drain tube 125 while the dirt G is adsorbed.

実施の形態5.
図10は、本発明の更に他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。同図に示す汚れ分解部90Dは、二次側循環管路の戻り管70bに中空円板状の大径の電極ホルダ部67dが形成された追焚き機能付き給湯機に取り付けられるものであり、軸部83d1と該軸部83d1に取り付けられたハニカム構造の電極部83d2とを有するプラス電極83d、およびメッシュ状のマイナス電極(図示せず)を備えている。なお、以下の説明では、ハニカム構造の電極部を「ハニカム構造電極部」という。
Embodiment 5 FIG.
FIG. 10 is a perspective view schematically showing a soil decomposing portion in still another bath water soil decomposing apparatus of the present invention. The dirt decomposing portion 90D shown in the figure is attached to a hot water supply device with a chasing function in which a hollow disk-like large-diameter electrode holder portion 67d is formed on the return pipe 70b of the secondary side circulation conduit, and it includes the shaft portion 83d 1 and shaft portion plus electrode 83d with the electrode portion 83d 2 of the attached honeycomb structure 83d 1, and a mesh-like negative electrode (not shown). In the following description, the electrode portion having the honeycomb structure is referred to as “honeycomb structure electrode portion”.

ハニカム構造電極部83d2は、セラミックスや合成樹脂等により作製される基材の表面に吸着剤としてのゼオライトと酸化触媒とを担持させて導電性をも付与したものであり、六角形状の各孔Hの軸線が軸部83d1の長手軸から僅かにずれるように成形されている。当該ハニカム構造電極部83d2は、各孔Hが浴水の流路となる向きで電極ホルダ部67dでのホルダ本体67d1に保持される。このとき、軸部83d1はホルダ本体67d1をその厚さ方向に貫通する。戻り管70bに浴水が流れると、ハニカム構造電極部83d2での各孔Hの軸線が軸部83d1の長手軸から僅かにずれていることから、浴水の流量に応じた速度でハニカム構造電極部83d2が軸部83d1を中心にして自然に回転する。マイナス電極は、ホルダ本体67d1の上部に取り外し可能に装着されるキャップ67d2の内側上部に配置される。 The honeycomb structure electrode portion 83d 2 is formed by supporting zeolite and an oxidation catalyst as adsorbents on the surface of a base material made of ceramics, synthetic resin, etc., and imparting conductivity to each of hexagonal holes. the axis of the H is shaped to deviate slightly from the longitudinal axis of the shaft portion 83d 1. The honeycomb structured electrode portions 83d 2, each hole H is held by the holder main body 67d 1 in orientation at the electrode holder portion 67d which is a flow path for the bath water. At this time, the shaft portion 83d 1 passes through the holder body 67d 1 in the thickness direction. When the bath water flows into the return pipe 70b, the axis of each hole H in the honeycomb structure electrode portion 83d 2 is slightly shifted from the longitudinal axis of the shaft portion 83d 1 , so that the honeycomb has a speed corresponding to the flow rate of the bath water. The structural electrode portion 83d 2 naturally rotates around the shaft portion 83d 1 . The minus electrode is arranged on the inner upper portion of the cap 67d 2 that is detachably mounted on the upper portion of the holder body 67d 1 .

図11は、図10に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。同図に示す例は、二次側循環管路の戻り管70bに上述の電極ホルダ部67dが形成された追焚き機能付き給湯機に図10の汚れ分解部90Dを配置した例であり、戻り管70bおよび浴水汚れ分解装置(図示せず)の各々を除いた追焚き機能付き給湯機の構成は、図1に示した追焚き機能付き給湯機130の構成と同様である。図11に示した構成要素のうちで図10に示した構成要素と共通するものについては、図10で用いた参照符号と同じ参照符号を付してその説明を省略する。図示を省略した浴水汚れ分解装置は、上述した汚れ分解部90Dの他に、汚れ分解部90D内のプラス電極83dとマイナス電極85dとに電圧を印加して放電を生じさせる電源部と、該電源部の出力動作を制御する電源制御部とを備えている。   FIG. 11 is a conceptual diagram schematically illustrating an example of a usage pattern of the dirt decomposing unit illustrated in FIG. 10. The example shown in the figure is an example in which the soil disassembling unit 90D of FIG. 10 is arranged in a water heater with a reheating function in which the electrode holder portion 67d described above is formed on the return pipe 70b of the secondary side circulation pipeline, The configuration of the hot water heater with a reheating function excluding each of the pipe 70b and the bath water dirt decomposing apparatus (not shown) is the same as that of the hot water heater 130 with a reheating function shown in FIG. Among the constituent elements shown in FIG. 11, those common to the constituent elements shown in FIG. 10 are given the same reference numerals as those used in FIG. 10, and description thereof is omitted. In addition to the above-described soil decomposing unit 90D, the bath water soil decomposing device not shown in the figure includes a power supply unit that applies a voltage to the positive electrode 83d and the negative electrode 85d in the soil decomposing unit 90D to generate a discharge, A power supply control unit that controls the output operation of the power supply unit.

図11中の上側の図に示すように、追焚き運転が開始されるのと同時に、浴水汚れ分解装置での電源部のプラス端子91aからプラス電極83dに所定の電圧が印加されて、プラス電極83dの極性がプラスに保たれる。マイナス電極85dには電圧が印加されない。その結果として、汚れGが吸着した微小泡MBがプラス電極83dに電気的に吸引されて、プラス電極83d表面での微小泡BMの密度が高まる。また、浴水150aが戻り管70bを流れることから、ハニカム構造電極部83d2が軸部83d1を中心にして1分間に1回転程度の速度で自然に回転する。 As shown in the upper diagram in FIG. 11, at the same time as the chasing operation is started, a predetermined voltage is applied from the positive terminal 91a of the power supply unit to the positive electrode 83d in the bath water dirt decomposing apparatus, The polarity of the electrode 83d is kept positive. No voltage is applied to the negative electrode 85d. As a result, the micro bubbles MB on which the dirt G is adsorbed are electrically attracted to the plus electrode 83d, and the density of the micro bubbles BM on the surface of the plus electrode 83d is increased. In addition, since the bath water 150a flows through the return pipe 70b, the honeycomb structure electrode portion 83d 2 naturally rotates at a speed of about one rotation per minute around the shaft portion 83d 1 .

図11中の下側の図に示すように、ハニカム構造電極部83d2が半回転すると、電源部のプラス端子91aおよびマイナス端子91bの各々から汚れ分解部90Cに所定のパルス放電電圧が印加され、プラス電極83dとマイナス電極85dとの間にパルス放電が生じて、微小泡MBに吸着していた汚れGが無害で極微小な有機物に分解される。パルス放電は、例えば追焚き運転の期間中、間欠的に行われる。浴水150a中の汚れGを上記の有機物に分解する結果として、浴水150aが清浄化される。なお、ハニカム構造電極部83d2の回転量は、図示を省略したロータリエンコーダにより検出され、該ロータリエンコーダの検出量に基づいて、浴水汚れ分解装置の電源制御部が電源部から各電極83d,85dへのパルス放電電圧の印加時期を判断する。 As shown in the lower diagram in FIG. 11, when the honeycomb structure electrode portion 83d 2 is rotated halfway, a predetermined pulse discharge voltage is applied from the positive terminal 91a and the negative terminal 91b of the power supply portion to the dirt decomposition portion 90C. A pulse discharge is generated between the plus electrode 83d and the minus electrode 85d, and the dirt G adsorbed on the microbubbles MB is decomposed into harmless and extremely fine organic substances. For example, the pulse discharge is intermittently performed during the chasing operation. As a result of decomposing the dirt G in the bath water 150a into the above organic substances, the bath water 150a is cleaned. Note that the rotation amount of the honeycomb structure electrode portion 83d 2 is detected by a rotary encoder (not shown), and based on the detection amount of the rotary encoder, the power control unit of the bath water dirt decomposing apparatus supplies each electrode 83d, The application timing of the pulse discharge voltage to 85d is determined.

実施の形態6.
図12は、本発明の更に他の浴水汚れ分解装置での汚れ分解部を示す概略図である。同図に示す汚れ分解部90Eは、紫外線照射部95を備えた浴水汚れ分解装置(図示せず)を構成するものであり、当該汚れ分解部90Eは、プラス電極83eを構成するハニカム構造電極部83e2での六角形状の各孔の軸線が軸部83e1の長手軸と略平行である点、および軸部83e1が駆動部87、具体的にはモータにより回転されてハニカム構造電極部83e2が回転する点をそれぞれ除き、図10に示した汚れ分解部90Dと同様の構成を有している。ただし、ハニカム構造電極部83e2には、吸着剤としてのゼオライトと、酸化触媒としてのプラチナ担持酸化チタンとが添着されている。
Embodiment 6 FIG.
FIG. 12 is a schematic view showing a soil decomposing unit in still another bath water soil decomposing apparatus of the present invention. The soil decomposing unit 90E shown in the figure constitutes a bath water soil decomposing device (not shown) provided with an ultraviolet irradiation unit 95, and the soil decomposing unit 90E is a honeycomb structure electrode constituting the plus electrode 83e. point axis of the hexagonal each hole in the part 83e 2 is substantially parallel to the longitudinal axis of the shaft portion 83e 1, and the shaft portion 83e 1 driving unit 87, in particular is rotated by a motor honeycomb structure electrode portion Except for the fact that 83e 2 rotates, it has the same configuration as the dirt decomposing portion 90D shown in FIG. However, the honeycomb structure electrode portion 83e 2 is attached with zeolite as an adsorbent and platinum-supported titanium oxide as an oxidation catalyst.

上記の汚れ分解部90Eは、二次側循環管路の戻り管70bに中空円板状を呈する大径の電極ホルダ部67eが形成された追焚き機能付き給湯機に取り付けられるものであり、電極ホルダ部67eは、プラス電極83eを回転可能に保持するホルダ本体67e1と、ホルダ本体67e1の上部に取り外し可能に装着されるキャップ67e2とにより構成される。キャップ67e2の所定箇所には紫外線透過窓Wが形成されており、マイナス電極85eはキャップ67e2の内側上部に配置される。戻り管70bおよび浴水汚れ分解装置の各々を除いた追焚き機能付き給湯機の構成は、図1に示した追焚き機能付き給湯機130の構成と同様である。図示を省略した浴水汚れ分解装置は、上述した汚れ分解部90Eおよび紫外線照射部95の他に、プラス電極83eとマイナス電極85eとに電圧を印加して放電を生じさせる電源部と、該電源部の出力動作を制御する電源制御部とを備えている。 The dirt decomposing portion 90E is attached to a hot water supply device with a chasing function in which a large-diameter electrode holder portion 67e having a hollow disk shape is formed in the return pipe 70b of the secondary-side circulation conduit. The holder portion 67e includes a holder main body 67e 1 that rotatably holds the plus electrode 83e, and a cap 67e 2 that is detachably attached to the upper portion of the holder main body 67e 1 . An ultraviolet transmissive window W is formed at a predetermined position of the cap 67e 2 , and the negative electrode 85e is disposed on the inner upper portion of the cap 67e 2 . The configuration of the hot water heater with a tracking function excluding each of the return pipe 70b and the bath water dirt decomposing apparatus is the same as the configuration of the hot water heater with a tracking function 130 shown in FIG. In addition to the soil decomposing unit 90E and the ultraviolet irradiation unit 95, the bath water soil decomposing device (not shown) includes a power source unit that generates a discharge by applying a voltage to the positive electrode 83e and the negative electrode 85e, and the power source. And a power supply control unit for controlling the output operation of the unit.

図12中の上側の図に示すように、追焚き運転が開始されるのと同時に、浴水汚れ分解装置での電源部のプラス端子91aからプラス電極83eに所定の電圧が印加されて、プラス電極83eの極性がプラスに保たれる。マイナス電極85eには電圧が印加されない。その結果として、汚れGが吸着した微小泡MBがプラス電極83eに電気的に吸引されて、プラス電極83e表面での微小泡BMの密度が高まる。また、駆動部87が起動され、ハニカム構造電極部83e2が軸部83e1を中心にして1時間に1回転程度の速度でゆっくり回転する。 As shown in the upper diagram in FIG. 12, at the same time as the chasing operation is started, a predetermined voltage is applied from the plus terminal 91a of the power supply unit to the plus electrode 83e in the bath water dirt decomposing apparatus, and plus The polarity of the electrode 83e is kept positive. No voltage is applied to the negative electrode 85e. As a result, the micro bubbles MB on which the dirt G is adsorbed are electrically attracted to the plus electrode 83e, and the density of the micro bubbles BM on the surface of the plus electrode 83e is increased. Further, the drive unit 87 is activated, and the honeycomb structure electrode unit 83e 2 rotates slowly at a speed of about one rotation per hour around the shaft unit 83e 1 .

図12中の下側の図に示すように、ハニカム構造電極部83e2が半回転すると、浴水汚れ分解装置での電源部のプラス端子91aおよびマイナス端子91bの各々から汚れ分解部90Eに所定のパルス放電電圧が印加されてプラス電極83eとマイナス電極85eとの間にパルス放電が生じ、浴水150a中の汚れGが無害で極微小な有機物に分解される。その結果として、浴水150aが清浄化される。また、紫外線照射部95の紫外光源95bが点灯される。同図においては、紫外光源95bから放射される紫外光を実線の矢印で表している。 As shown in the lower diagram in FIG. 12, when the honeycomb structure electrode portion 83e 2 is rotated halfway, a predetermined value is supplied from the positive terminal 91a and the negative terminal 91b of the power supply unit to the soil decomposition unit 90E. The pulse discharge voltage is applied to generate a pulse discharge between the plus electrode 83e and the minus electrode 85e, and the dirt G in the bath water 150a is decomposed into harmless and extremely fine organic substances. As a result, the bath water 150a is cleaned. Further, the ultraviolet light source 95b of the ultraviolet irradiation unit 95 is turned on. In the figure, the ultraviolet light emitted from the ultraviolet light source 95b is represented by a solid line arrow.

紫外光源95bからの紫外光によってハニカム構造電極部83e2中の酸化触媒の酸化作用が助長されることから、図示の使用形態の下では、紫外光を照射しない場合に比べ、汚れGの分解速度が1.5倍程度速くなり、これに伴ってパルス放電電圧の総印加時間を70%程度に低減させることが可能になる。なお、ハニカム構造電極部83e2の回転量は、図示を省略したロータリエンコーダにより検出され、該ロータリエンコーダの検出量に基づいて、浴水汚れ分解装置の電源制御部が電源部から各電極83e,85eへのパルス放電電圧の印加時期を判断する。 Since the oxidation action of the oxidation catalyst in the honeycomb structure electrode portion 83e 2 is promoted by the ultraviolet light from the ultraviolet light source 95b, the decomposition rate of the dirt G is lower than that in the case where the ultraviolet light is not irradiated under the usage pattern shown in the figure. Accordingly, the total application time of the pulse discharge voltage can be reduced to about 70%. Note that the rotation amount of the honeycomb structure electrode portion 83e 2 is detected by a rotary encoder (not shown), and based on the detection amount of the rotary encoder, the power control unit of the bath water dirt decomposing apparatus supplies each electrode 83e, The application timing of the pulse discharge voltage to 85e is determined.

実施の形態7.
図13は、本発明の更に他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。同図に示す汚れ分解部90Fは、2つのマイナス電極85fを有するという点を除き、図12に示した汚れ分解部90Eと同様の構成を有している。ただし、ハニカム構造電極部83f2には、吸着剤として活性炭が添着されている。図13においては、汚れ分解部90Fでのプラス電極に参照符号「83f」を付し、該プラス電極83fでの軸部に参照符号「83f1」を付し、該プラス電極83fでのハニカム構造電極部に参照符号「83f2」を付してある。
Embodiment 7 FIG.
FIG. 13 is a perspective view schematically showing a soil decomposing portion in still another bath water soil decomposing apparatus of the present invention. The dirt decomposing unit 90F shown in the figure has the same configuration as the dirt decomposing unit 90E shown in FIG. 12 except that it has two negative electrodes 85f. However, the honeycomb structure electrode portion 83f 2 is attached with activated carbon as an adsorbent. In FIG. 13, the reference sign “83f” is attached to the plus electrode in the soil decomposition part 90F, the reference sign “83f 1 ” is attached to the shaft part in the plus electrode 83f, and the honeycomb structure in the plus electrode 83f Reference numeral “83f 2 ” is attached to the electrode portion.

この汚れ分解部90Fは、二次側循環管路の戻り管70bに中空円板状の大径の電極ホルダ部67fが形成された追焚き機能付き給湯機に取り付けられる。図示の電極ホルダ部67fは、図10に示した電極ホルダ部67dと同様に、プラス電極83fを回転可能に保持するホルダ本体67f1と、該ホルダ本体67f1の上部に取り外し可能に装着されるキャップ67f2とを有している。キャップ67f2には、オゾン水生成装置96aが生成したオゾン水の流入路となる配管96bと、上記オゾン水の排出流路となるドレイン管125とが接続されており、当該キャップ67f2内での配管96dとの接続箇所に1つのマイナス電極85fが、また当該キャップ67f2内でのドレイン管125との接続箇所に他のマイナス電極85fがそれぞれ配置されている。なお、オゾン水生成装置96aと配管96bとは、汚れ分解部90Fと共に浴水汚れ分解装置を構成する。 The dirt decomposing unit 90F is attached to a hot water supply device with a chasing function in which a return electrode 70b of the secondary-side circulation conduit is formed with a hollow disk-like large-diameter electrode holder 67f. Electrode holder portion 67f shown, like the electrode holder portion 67d shown in FIG. 10, a holder main body 67f 1 for rotatably holding the positive electrode 83f, is removably mounted on the upper part of the holder body 67f 1 and a cap 67f 2. The cap 67f 2, a pipe 96b serving as inlet channel of the ozone water ozone water producing apparatus 96a is generated, and the drain pipe 125 as a discharge flow path of the ozone water is connected, in the cap 67f within 2 one negative electrodes 85f at connection points between the pipe 96d of, also other negative electrodes 85f at connection points between the drain tube 125 in the cap 67f within 2 are arranged. The ozone water generating device 96a and the pipe 96b constitute a bath water soil decomposing device together with the soil decomposing unit 90F.

図14は、図13に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。同図に示す例は、二次側循環管路の戻り管70bに上述の電極ホルダ部67fが形成された追焚き機能付き給湯機に図13の汚れ分解部90Fを配置した例であり、戻り管70b、浴水汚れ分解装置(図示せず)、およびドレイン管125の各々を除いた追焚き機能付き給湯機の構成は、図1に示した追焚き機能付き給湯機130の構成と同様である。図14に示した構成要素のうちで図13に示した構成要素と共通するものについては、図13で用いた参照符号と同じ参照符号を付してその説明を省略する。図示を省略した浴水汚れ分解装置は、上述した汚れ分解部90F、オゾン水生成装置96a、および配管96bの他に、プラス電極83fとマイナス電極85fとに電圧を印加して放電を生じさせる電源部と、該電源部の出力動作を制御する電源制御部とを備えている。   FIG. 14 is a conceptual diagram schematically showing an example of a usage pattern of the dirt decomposing unit shown in FIG. The example shown in the figure is an example in which the soil decomposition unit 90F of FIG. 13 is arranged in a hot water supply device with a reheating function in which the electrode holder portion 67f described above is formed in the return pipe 70b of the secondary side circulation pipeline. The configuration of the water heater with a reheating function excluding each of the pipe 70b, the bath water dirt decomposing apparatus (not shown), and the drain pipe 125 is the same as that of the water heater 130 with a reheating function shown in FIG. is there. Among the constituent elements shown in FIG. 14, those common to the constituent elements shown in FIG. 13 are denoted by the same reference numerals as those used in FIG. 13, and description thereof is omitted. The bath water dirt decomposing apparatus (not shown) is a power source that generates a discharge by applying a voltage to the plus electrode 83f and the minus electrode 85f in addition to the dirt decomposing unit 90F, the ozone water generating apparatus 96a, and the pipe 96b. And a power supply control unit that controls the output operation of the power supply unit.

図14中の上側の図に示すように、追焚き運転が開始されるのと同時に、浴水汚れ分解装置での電源部のプラス端子91aからプラス電極83fに所定の電圧が印加されて、プラス電極83fの極性がプラスに保たれる。マイナス電極85fには電圧が印加されない。その結果として、汚れGが吸着した微小泡MBがプラス電極83fに電気的に吸引されて、プラス電極83f表面での微小泡BMの密度が高まる。ハニカム構造電極部83f2は、軸部83e1を中心にして1日に1回転程度の速度でゆっくり回転する。 As shown in the upper diagram in FIG. 14, at the same time as the chasing operation is started, a predetermined voltage is applied to the plus electrode 83f from the plus terminal 91a of the power supply unit in the bath water dirt decomposing apparatus, and plus The polarity of the electrode 83f is kept positive. No voltage is applied to the negative electrode 85f. As a result, the micro bubbles MB adsorbed with the dirt G are electrically attracted to the plus electrode 83f, and the density of the micro bubbles BM on the surface of the plus electrode 83f increases. The honeycomb structure electrode portion 83f 2 rotates slowly at a speed of about one rotation per day around the shaft portion 83e 1 .

図14中の下側の図に示すように、ハニカム構造電極部83e2が半回転すると、汚れ分解装置での電源部のプラス端子91aおよびマイナス端子91bの各々から汚れ分解部90Fに所定のパルス放電電圧が印加されて、プラス電極83eとマイナス電極85eとの間にパルス放電が生じる。また、パルス放電が開始されると、オゾン水生成装置96aから電極ホルダ部67fにオゾン水OWが供給される。 As shown in the lower diagram of FIG. 14, when the honeycomb structure electrode portion 83e 2 is rotated halfway, a predetermined pulse is supplied from each of the positive terminal 91a and the negative terminal 91b of the power source unit to the dirt decomposing unit 90F in the dirt decomposing apparatus. A discharge voltage is applied, and a pulse discharge is generated between the plus electrode 83e and the minus electrode 85e. When pulse discharge is started, ozone water OW is supplied from the ozone water generator 96a to the electrode holder 67f.

上記のオゾン水OWによりハニカム構造電極部83e2中の吸着剤の表面が清浄化されると共に、ハニカム構造電極部83e2での有機物の分解作用が助長されることから、図示の使用形態の下では、オゾン水OWを供給しない場合に比べ、汚れGの分解速度が2倍程度速くなり、これに伴ってパルス放電電圧の総印加時間を半分程度に低減させることが可能になる。電極ホルダ部67fに供給されたオゾン水OWは、ドレイン管125に排出される。図14中の下側の図においては、オゾン水OWの流れ方向を破線の矢印で示している。なお、ハニカム構造電極部83f2の回転量は、図示を省略したロータリエンコーダにより検出され、該ロータリエンコーダの検出量に基づいて、浴水汚れ分解装置の電源制御部が電源部から各電極83f,85fへのパルス放電電圧の印加時期を判断する。 Together with the surface of the adsorbent of the honeycomb structured electrode portion 83e 2 by the above ozone water OW it is cleaned, since the decomposition of organic matter in the honeycomb structure electrode portion 83e 2 is promoted under the usage pattern shown Then, compared with the case where ozone water OW is not supplied, the decomposition rate of the dirt G is about twice as fast, and accordingly, the total application time of the pulse discharge voltage can be reduced to about half. The ozone water OW supplied to the electrode holder portion 67f is discharged to the drain pipe 125. In the lower diagram in FIG. 14, the flow direction of the ozone water OW is indicated by broken-line arrows. Note that the rotation amount of the honeycomb structure electrode portion 83f 2 is detected by a rotary encoder (not shown), and based on the detection amount of the rotary encoder, the power supply control unit of the bath water dirt decomposing apparatus supplies each electrode 83f, The application timing of the pulse discharge voltage to 85f is determined.

実施の形態8.
図15は、本発明の更に他の浴水汚れ分解装置での汚れ分解部を示す概略図である。同図に示す汚れ分解部90Gは、微小泡含有水生成器97aを備えた浴水汚れ分解装置(図示せず)を構成するものであり、当該汚れ分解部90Gは、プラス電極83gを構成するハニカム構造電極部83g2での六角形状の各孔の軸線が軸部83g1の長手軸から僅かに傾いている点、および軸部83g1を回転させるモータを有していない点をそれぞれ除き、図14に示した汚れ分解部90Fと同様の構成を有している。
Embodiment 8 FIG.
FIG. 15 is a schematic view showing a soil decomposing portion in still another bath water soil decomposing apparatus of the present invention. The soil decomposing unit 90G shown in the figure constitutes a bath water soil decomposing device (not shown) provided with a microbubble-containing water generator 97a, and the soil decomposing unit 90G constitutes a positive electrode 83g. except that the axis of the hexagonal each hole in the honeycomb structure electrode portion 83 g 2 is slightly inclined from the longitudinal axis of the shaft portion 83 g 1, and the shaft portion 83 g 1 a that it does not have the motor which rotates respectively, The structure is the same as that of the dirt decomposing portion 90F shown in FIG.

上記の汚れ分解部90Gは、二次側循環管路の戻り管70bに中空円板状を呈する大径の電極ホルダ部67gが形成された追焚き機能付き給湯機に取り付けられるものであり、電極ホルダ部67gは、微小泡含有水生成器97aが生成した微小泡含有水の流入路となる配管97bとの接続口、および微小泡含有水の流出路となるドレイン管125との接続口がそれぞれ大径であるという点を除き、図14に示した電極ホルダ部67fと同様の構成を有している。戻り管70bおよび浴水汚れ分解装置の各々を除いた追焚き機能付き給湯機の構成は、図1に示した追焚き機能付き給湯機130の構成と同様である。図示を省略した浴水汚れ分解装置は、上述した汚れ分解部90G、微小泡含有水生成器97a、および配管97bの他に、プラス電極83gとマイナス電極85gとに電圧を印加して放電を生じさせる電源部と、該電源部の出力動作を制御する電源制御部とを備えている。   The dirt decomposing portion 90G is attached to a water heater with a reheating function in which a large-diameter electrode holder portion 67g having a hollow disk shape is formed in the return pipe 70b of the secondary-side circulation conduit, The holder portion 67g has a connection port with the pipe 97b that becomes an inflow path of the microbubble-containing water generated by the microbubble-containing water generator 97a and a connection port with the drain pipe 125 that becomes the outflow path of the microbubble-containing water. Except for the large diameter, it has the same configuration as the electrode holder portion 67f shown in FIG. The configuration of the hot water heater with a tracking function excluding each of the return pipe 70b and the bath water dirt decomposing apparatus is the same as the configuration of the hot water heater with a tracking function 130 shown in FIG. The bath water dirt decomposing apparatus (not shown) generates a discharge by applying a voltage to the plus electrode 83g and the minus electrode 85g in addition to the dirt decomposing unit 90G, the fine bubble-containing water generator 97a, and the pipe 97b. And a power supply control unit that controls the output operation of the power supply unit.

図15中の上側の図に示すように、追焚き運転が開始されるのと同時に、浴水汚れ分解装置での電源部のプラス端子91aからプラス電極83gに所定の電圧が印加されて、プラス電極83gの極性がプラスに保たれる。マイナス電極85gには電圧が印加されない。その結果として、汚れGが吸着した微小泡MBがプラス電極83gに電気的に吸引されて、プラス電極83g表面での微小泡BMの密度が高まる。また、浴水150aが戻り管70bを流れることから、ハニカム構造電極部83g2が軸部83g1を中心にして1分間に1回転程度の速度で自然に回転する。 As shown in the upper diagram in FIG. 15, at the same time as the chasing operation is started, a predetermined voltage is applied from the plus terminal 91a of the power supply unit to the plus electrode 83g in the bath water dirt decomposing apparatus, The polarity of the electrode 83g is kept positive. No voltage is applied to the negative electrode 85g. As a result, the fine bubbles MB adsorbed with the dirt G are electrically attracted to the positive electrode 83g, and the density of the fine bubbles BM on the surface of the positive electrode 83g is increased. Further, since the bath water 150a flows through the return pipe 70b, the honeycomb structure electrode portion 83g 2 naturally rotates at a speed of about one rotation per minute around the shaft portion 83g 1 .

図15中の下側の図に示すように、ハニカム構造電極部83g2が半回転すると、浴水汚れ分解装置での電源部のプラス端子91aおよびマイナス端子91bの各々から汚れ分解部90Gに所定のパルス放電電圧が印加され、プラス電極83gと各マイナス電極85gとの間にパルス放電が生じて、微小泡MBに吸着した汚れGが無害で極微小な有機物に分解される。その結果として、浴水150aが清浄化される。 As shown in the lower diagram in FIG. 15, when the honeycomb structure electrode portion 83g 2 is rotated halfway, a predetermined value is supplied from the positive terminal 91a and the negative terminal 91b of the power source unit to the soil decomposition unit 90G in the bath water soil decomposition device. The pulse discharge voltage is applied and a pulse discharge is generated between the positive electrode 83g and each negative electrode 85g, and the dirt G adsorbed on the microbubbles MB is harmlessly decomposed into extremely fine organic substances. As a result, the bath water 150a is cleaned.

また、パルス放電が開始されると、多数の微小泡mbを含有した微小泡含有水BWが微小泡含有水生成器97aから電極ホルダ部67gに供給される。この微小泡含有水BWは、主としてプラス電極83gおよびマイナス電極85gの表面の洗浄に利用される。微小泡含有水BWを電極ホルダ部67gに供給することにより、各電極83g,85gの表面を清浄に保つことが容易になる。電極ホルダ部67gに供給された微小泡含有水BWは、ドレイン管125に排出される。図14中の下側の図においては、微小泡含有水BWの流れ方向を一点鎖線の矢印で示している。なお、ハニカム構造電極部83g2の回転量は、図示を省略したロータリエンコーダにより検出され、該ロータリエンコーダの検出量に基づいて、浴水汚れ分解装置の電源制御部が電源部から各電極83g,85gへのパルス放電電圧の印加時期を判断する。 Moreover, when pulse discharge is started, the microbubble containing water BW containing many microbubbles mb is supplied to the electrode holder part 67g from the microbubble containing water generator 97a. The microbubble-containing water BW is mainly used for cleaning the surfaces of the positive electrode 83g and the negative electrode 85g. By supplying the microbubble-containing water BW to the electrode holder 67g, it becomes easy to keep the surfaces of the electrodes 83g and 85g clean. The microbubble-containing water BW supplied to the electrode holder portion 67g is discharged to the drain pipe 125. In the lower diagram in FIG. 14, the flow direction of the fine bubble-containing water BW is indicated by a one-dot chain line arrow. Note that the rotation amount of the honeycomb structure electrode portion 83g 2 is detected by a rotary encoder (not shown), and based on the detection amount of the rotary encoder, the power supply control unit of the bath water dirt decomposing apparatus sends each electrode 83g, The application timing of the pulse discharge voltage to 85 g is determined.

実施の形態9.
図16は、本発明の更に他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。同図に示す汚れ分解部90Hは、軸部83h1と該軸部83h1に取り付けられたハニカム構造電極部83h2とを有するプラス電極83h、およびハニカム状のマイナス電極85hを備えており、ハニカム構造電極部83h2とマイナス電極85hとは、軸部83h1に一定間隔で交互に取り付けられている。ハニカム構造電極部83h2およびマイナス電極85hの各々は、セラミックスや合成樹脂等により作製される基材の表面に吸着剤としてのゼオライトおよび酸化触媒等を添着させて導電性をも付与したものであり、当該ハニカム構造電極部83h2およびマイナス電極85hの各々は、六角形状の各孔Hの軸線が軸部83h1の長手軸から僅かにずれるように成形されている。
Embodiment 9 FIG.
FIG. 16 is a perspective view schematically showing a soil decomposing portion in still another bath water soil decomposing apparatus of the present invention. Dirt decomposing unit 90H shown in the figure, provided with positive electrodes 83h and a shaft portion 83h 1 and shaft portion 83h honeycomb structured electrode portions 83h 2 attached to the 1, and the honeycomb negative electrode 85h, honeycomb The structural electrode portions 83h 2 and the negative electrodes 85h are alternately attached to the shaft portion 83h 1 at regular intervals. Each of the honeycomb structure electrode portion 83h 2 and the negative electrode 85h is provided with conductivity by adding zeolite, an oxidation catalyst, or the like as an adsorbent to the surface of a base material made of ceramics or synthetic resin. Each of the honeycomb structure electrode portion 83h 2 and the negative electrode 85h is formed such that the axis of each hexagonal hole H is slightly shifted from the longitudinal axis of the shaft portion 83h 1 .

この汚れ分解部90Hは、二次側循環管路の戻り管70bに中空円板状の大径の電極ホルダ部67hが形成された追焚き機能付き給湯機に取り付けられる。図示の電極ホルダ部67hは、プラス電極83hおよびマイナス電極85hを回転可能に保持するホルダ本体67h1と、該ホルダ本体67h1の上部に取り外し可能に装着されるキャップ67h2とを有している。 The dirt decomposing portion 90H is attached to a hot water supply device with a chasing function in which a return electrode 70b of the secondary side circulation conduit is formed with a hollow disk-like large-diameter electrode holder portion 67h. Electrode holder portion 67h shown includes a holder body 67h 1 for rotatably holding the positive electrode 83h and the negative electrode 85h, and a cap 67h 2 which is detachably mounted to the upper portion of the holder main body 67h 1 .

図17は、図16に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。同図に示す例は、二次側循環管路の戻り管70bに上述の電極ホルダ部67hが形成された追焚き機能付き給湯機に図16の汚れ分解部90Hを配置した例であり、戻り管70bおよび浴水汚れ分解装置(図示せず)の各々を除いた追焚き機能付き給湯機の構成は、図1に示した追焚き機能付き給湯機130の構成と同様である。図17に示した構成要素のうちで図16に示した構成要素と共通するものについては、図16で用いた参照符号と同じ参照符号を付してその説明を省略する。図示を省略した浴水汚れ分解装置は、上述した汚れ分解部90Hの他に、プラス電極83hとマイナス電極85hとに電圧を印加して放電を生じさせる電源部と、該電源部の出力動作を制御する電源制御部とを備えている。   FIG. 17 is a conceptual diagram schematically showing an example of a usage pattern of the dirt decomposing unit shown in FIG. The example shown in the figure is an example in which the soil decomposition unit 90H of FIG. 16 is arranged in a hot water supply device with a reheating function in which the electrode holder portion 67h is formed on the return pipe 70b of the secondary side circulation line. The configuration of the hot water heater with a reheating function excluding each of the pipe 70b and the bath water dirt decomposing apparatus (not shown) is the same as that of the hot water heater 130 with a reheating function shown in FIG. Of the constituent elements shown in FIG. 17, those common to the constituent elements shown in FIG. 16 are assigned the same reference numerals as those used in FIG. 16, and descriptions thereof are omitted. In addition to the above-described soil decomposing unit 90H, the bath water soil decomposing device, which is not shown, applies a voltage to the positive electrode 83h and the negative electrode 85h to cause discharge, and an output operation of the power unit. And a power control unit for controlling.

図17中の上側の図に示すように、追焚き運転が開始されるのと同時に、浴水汚れ分解装置での電源部のプラス端子91aからプラス電極83hに所定の電圧が印加されて、プラス電極83hの極性がプラスに保たれる。マイナス電極85hには電圧が印加されない。その結果として、汚れGが吸着した微小泡MBがプラス電極83hに電気的に吸引されて、プラス電極83h表面での微小泡BMの密度が高まる。各ハニカム構造電極部83h2および各マイナス電極85hは、軸部83e1を中心にして1分間に1回転程度の速度で自然に回転する。 As shown in the upper diagram in FIG. 17, at the same time as the chasing operation is started, a predetermined voltage is applied from the plus terminal 91a of the power supply unit to the plus electrode 83h in the bath water dirt decomposing apparatus, The polarity of the electrode 83h is kept positive. No voltage is applied to the negative electrode 85h. As a result, the micro bubbles MB adsorbed with the dirt G are electrically attracted to the plus electrode 83h, and the density of the micro bubbles BM on the surface of the plus electrode 83h is increased. Each honeycomb structure electrode portion 83h 2 and each minus electrode 85h naturally rotate at a speed of about one rotation per minute around the shaft portion 83e 1 .

図17中の下側の図に示すように、各ハニカム構造電極部83h2および各マイナス電極85hが半回転すると、汚れ分解装置での電源部のプラス端子91aおよびマイナス端子91bの各々から汚れ分解部90Fに所定のパルス放電電圧が印加され、プラス電極83hとマイナス電極85hとの間にパルス放電が生じて、微小泡MBに吸着していた汚れGが無害で極微小な有機物に分解される。結果として、浴水150aは清浄化される。 As shown in the lower diagram in FIG. 17, when each honeycomb structure electrode portion 83h 2 and each negative electrode 85h are rotated halfway, the soil is decomposed from each of the positive terminal 91a and the negative terminal 91b of the power source portion in the soil decomposition apparatus. A predetermined pulse discharge voltage is applied to the portion 90F, and a pulse discharge is generated between the plus electrode 83h and the minus electrode 85h, and the dirt G adsorbed on the microbubbles MB is harmlessly decomposed into extremely fine organic substances. . As a result, the bath water 150a is cleaned.

この汚れ分解部90Hでは、ハニカム構造電極部83h2とマイナス電極85hとが交互に配置されているので、放電が生じる電極表面の面積が実施の形態5〜8で挙げた汚れ分解部に比べて増加しており、汚れGを効率よく分解することができる。また、ハニカム構造電極部83h2およびマイナス電極85hの厚みを薄くして電極間距離を近づければ、プラス電極83hおよびマイナス電極85hに供給するパルス放電電圧を下げても汚れGを効率よく分解することができる。なお、ハニカム構造電極部83h2およびマイナス電極85hの回転量は、図示を省略したロータリエンコーダにより検出され、該ロータリエンコーダの検出量に基づいて、浴水汚れ分解装置の電源制御部が電源部から各電極83h,85hへのパルス放電電圧の印加時期を判断する。 In this dirt decomposition part 90H, since the honeycomb structure electrode parts 83h 2 and the negative electrodes 85h are alternately arranged, the area of the electrode surface where discharge occurs is larger than that of the dirt decomposition part described in the fifth to eighth embodiments. The dirt G can be efficiently decomposed. Moreover, if the thickness of the honeycomb structure electrode portion 83h 2 and the negative electrode 85h is reduced and the distance between the electrodes is reduced, the dirt G is efficiently decomposed even if the pulse discharge voltage supplied to the positive electrode 83h and the negative electrode 85h is lowered. be able to. Note that the rotation amounts of the honeycomb structure electrode portion 83h 2 and the minus electrode 85h are detected by a rotary encoder (not shown), and based on the detection amount of the rotary encoder, the power control unit of the bath water dirt decomposing apparatus The application timing of the pulse discharge voltage to each electrode 83h, 85h is determined.

以上、本発明の浴水汚れ分解装置および追焚き機能付き給湯機について実施の形態を挙げて説明したが、前述のように、本発明は上記の形態に限定されるものではない。例えば、浴水汚れ分解装置における電源制御部は必須の構成部材ではなく、追焚き機能付き給湯機の制御部に当該電源制御部を兼ねさせることも可能である。浴水汚れ分解装置における微小泡発生部も必須の構成部材ではなく、任意の構成部材とすることができるが、追焚き用の配管を流れる浴水中の汚れを効率よく分解するうえからは、微小泡発生部を用いて浴水汚れ分解装置を構成した方が好ましい。また、実施の形態1〜9では、汚れ分解部の各電極を保持する電極ホルダ部を追焚き機能付き給湯機における二次側循環管路での戻り管の一部として説明したが、電極ホルダ部は浴水汚れ分解装置の一構成部材とみなすこともできる。   As described above, the embodiment of the bath water dirt decomposing apparatus and the hot water supply device with a chasing function of the present invention has been described. However, as described above, the present invention is not limited to the above embodiment. For example, the power supply control unit in the bath water dirt decomposing apparatus is not an essential component, and the control unit of the water heater with a reheating function can also serve as the power supply control unit. The micro-bubble generating part in the bath water dirt decomposing apparatus is not an indispensable constituent member and can be an arbitrary constituent member. However, in order to efficiently decompose the dirt in the bath water flowing through the piping for chasing, the micro-bubble generating part is very small. It is preferable to configure the bath water dirt decomposing apparatus using the foam generating part. In the first to ninth embodiments, the electrode holder portion that holds each electrode of the dirt decomposition portion has been described as a part of the return pipe in the secondary side circulation line in the hot water heater with a tracking function. The part can also be regarded as a component of the bath water dirt decomposing apparatus.

汚れ分解部のプラス電極およびマイナス電極の材料は、適宜選定可能である。チタンやタングステン等の単体金属より各電極を作製することもできるし、ステンレス等の合金により各電極を作製することもできるし、単体金属製または合金製の基材にプラチナ、銀、金等をコーティングすることで各電極を作製することもできる。さらには、金属、セラミックス、合成樹脂等により作製した基材の表面に酸化チタン、酸化マンガン、またはこれらの表面にプラチナ等の貴金属を担持させた酸化触媒、およびゼオライト、活性炭等の吸着剤の少なくとも一方を添着させて各電極を作製することもできる。   The material of the plus electrode and the minus electrode of the soil decomposition part can be selected as appropriate. Each electrode can be made from a single metal such as titanium or tungsten, each electrode can be made from an alloy such as stainless steel, and platinum, silver, gold, etc. can be applied to a single metal or alloy base material. Each electrode can also be produced by coating. Furthermore, the surface of the base material made of metal, ceramics, synthetic resin or the like, titanium oxide, manganese oxide, or an oxidation catalyst having noble metal such as platinum supported on these surfaces, and at least an adsorbent such as zeolite or activated carbon One electrode can be attached to each electrode.

汚れ分解部でのプラス電極とマイナス電極との電極間距離は、20mm程度以下の範囲内で適宜選定可能であり、概ね5〜20mm以下とすることが好ましい。また、プラス電極とマイナス電極とに印加する電圧は、数十kV程度以下の範囲内で適宜選定可能であり、概ね1kV〜30kVの範囲内とすることもできる。当該汚れ分解部が取り付けられる追焚き機能付き給湯機は、ヒートポンプユニットにより湯を沸き上げるタイプのものの他に、貯湯タンク内に配置したヒータにより湯を沸き上げるタイプのものであってもよい。本発明については、上述した以外にも種々の変形、修飾、組み合わせ等が可能である。   The interelectrode distance between the plus electrode and the minus electrode in the soil decomposition part can be appropriately selected within a range of about 20 mm or less, and is preferably about 5 to 20 mm or less. In addition, the voltage applied to the plus electrode and the minus electrode can be appropriately selected within a range of about several tens of kV or less, and can be generally within a range of 1 kV to 30 kV. The hot water heater with a reheating function to which the dirt decomposing unit is attached may be of a type in which hot water is heated by a heater disposed in a hot water storage tank, in addition to a type in which hot water is heated by a heat pump unit. The present invention can be variously modified, modified and combined in addition to the above.

本発明の浴水汚れ分解装置は、家庭用または業務用の追焚き機能付き給湯機に用いることができ、本発明の追焚き機能付き給湯機は、家庭用または業務用の給湯機として用いることができる。   The bathing water dirt decomposing apparatus of the present invention can be used for a hot water heater with a reheating function for home use or business use, and the hot water heater with a reheating function of the present invention can be used as a hot water supply apparatus for home use or business use. Can do.

本発明の追焚き機能付き給湯機の一例を示す概略図である。It is the schematic which shows an example of the hot water supply machine with a chasing function of this invention. 図1に示した追焚き機能付き給湯機を構成している浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。It is a perspective view which shows roughly the stain | pollution | contamination decomposition | disassembly part in the bath water stain | pollution | contamination decomposition | disassembly apparatus which comprises the water heater with a chasing function shown in FIG. 図2に示した汚れ分解部による汚れの分解を概略的に示す概念図である。It is a conceptual diagram which shows roughly decomposition | disassembly of the dirt by the dirt decomposition | disassembly part shown in FIG. 本発明の他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。It is a perspective view which shows roughly the soil decomposition | disassembly part in the other bath water soil decomposition | disassembly apparatus of this invention. 図4に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。It is a conceptual diagram which shows roughly an example of the usage pattern of the dirt decomposition | disassembly part shown in FIG. 図4に示した汚れ分解部の使用形態の他の例を概略的に示す概念図である。It is a conceptual diagram which shows roughly the other example of the usage pattern of the dirt decomposition | disassembly part shown in FIG. 本発明の更に他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。It is a perspective view which shows roughly the soil decomposition | disassembly part in the further another bath water soil decomposition | disassembly apparatus of this invention. 図7に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。It is a conceptual diagram which shows roughly an example of the usage condition of the dirt decomposition | disassembly part shown in FIG. 図7に示した汚れ分解部の使用形態の他の例を概略的に示す概念図である。It is a conceptual diagram which shows roughly the other example of the usage pattern of the dirt decomposition | disassembly part shown in FIG. 本発明の更に他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。It is a perspective view which shows roughly the soil decomposition | disassembly part in the further another bath water soil decomposition | disassembly apparatus of this invention. 図10に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。It is a conceptual diagram which shows roughly an example of the usage pattern of the dirt decomposition | disassembly part shown in FIG. 本発明の更に他の浴水汚れ分解装置での汚れ分解部を示す概略図である。It is the schematic which shows the soil decomposition | disassembly part in the further another bath water soil decomposition | disassembly apparatus of this invention. 本発明の更に他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。It is a perspective view which shows roughly the soil decomposition | disassembly part in the further another bath water soil decomposition | disassembly apparatus of this invention. 図13に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。It is a conceptual diagram which shows roughly an example of the usage condition of the dirt decomposition | disassembly part shown in FIG. 本発明の更に他の浴水汚れ分解装置での汚れ分解部を示す概略図である。It is the schematic which shows the soil decomposition | disassembly part in the further another bath water soil decomposition | disassembly apparatus of this invention. 本発明の更に他の浴水汚れ分解装置での汚れ分解部を概略的に示す斜視図である。It is a perspective view which shows roughly the soil decomposition | disassembly part in the further another bath water soil decomposition | disassembly apparatus of this invention. 図16に示した汚れ分解部の使用形態の一例を概略的に示す概念図である。It is a conceptual diagram which shows roughly an example of the usage pattern of the dirt decomposition | disassembly part shown in FIG.

符号の説明Explanation of symbols

20 貯湯タンク
60 一次側循環管路
60a 往き管
60b 戻り管
67a,67b,67d〜67h 電極ホルダ部
70 二次側循環管路
70a 往き管
70b 戻り管
80 追焚き用熱交換器
83a〜83h プラス電極
83d2,83e2,83f2,83g2,83h2 ハニカム構造の電極部
85a〜85h マイナス電極
87 駆動部
90A〜90H 汚れ分解部
91 電源部
92 電源制御部
93 微小泡発生部
100 浴水汚れ分解装置
130 追焚き機能付き給湯機
150 浴槽
150a 浴水
MB 微小泡
G 汚れ
DESCRIPTION OF SYMBOLS 20 Hot water storage tank 60 Primary side circulation pipe 60a Outward pipe 60b Return pipe 67a, 67b, 67d-67h Electrode holder part 70 Secondary side circulation pipe 70a Outward pipe 70b Return pipe 80 Heating exchanger 83a-83h for reheating 83d 2 , 83e 2 , 83f 2 , 83g 2 , 83h 2 Honeycomb structure electrode part 85a to 85h Negative electrode 87 Drive part 90A to 90H Dirt decomposition part 91 Power supply part 92 Power supply control part 93 Microbubble generation part 100 Bath water dirt decomposition Device 130 Water heater with chasing function 150 Bath 150a Bath water MB Micro bubbles G Dirt

Claims (10)

浴槽から浴水を取り出して加熱した後に前記浴槽に戻す追焚き機能付き給湯機での追焚き用の配管に取り付けられる浴水汚れ分解装置であって、
前記追焚き用の配管内に配置されるプラス電極およびマイナス電極と、
前記プラス電極と前記マイナス電極とに電圧を印加して、該プラス電極と該マイナス電極との間に放電を生じさせる電源部と、
を備え、前記追焚き用の配管を流れる浴水中の汚れを前記放電により分解することを特徴とする浴水汚れ分解装置。
A bathing water decomposing apparatus attached to piping for reheating in a hot water heater with a reheating function that takes out the bath water from the bathtub and heats it back to the bathtub.
A positive electrode and a negative electrode disposed in the piping for reheating,
A power supply unit that applies a voltage to the plus electrode and the minus electrode to generate a discharge between the plus electrode and the minus electrode;
The bath water dirt decomposing apparatus is characterized in that dirt in bath water flowing through the piping for chasing is decomposed by the discharge.
前記追焚き用の配管での前記プラス電極および前記マイナス電極の上流側に配置されて、前記配管を流れる浴水中に微小泡を発生させる微小泡発生部を更に備え、
前記微小泡に吸着した汚れを前記放電により分解することを特徴とする請求項1に記載の浴水汚れ分解装置。
A micro-bubble generating part that is arranged on the upstream side of the plus electrode and the minus electrode in the tracking pipe and that generates micro-bubbles in the bath water flowing through the pipe;
2. The bath water dirt decomposing apparatus according to claim 1, wherein the dirt adsorbed on the micro bubbles is decomposed by the discharge.
前記汚れが吸着した微小泡を前記プラス電極で電気的に吸引した後、前記汚れを前記放電により分解することを特徴とする請求項2に記載の浴水汚れ分解装置。   3. The bath water dirt decomposing apparatus according to claim 2, wherein the dirt is decomposed by the discharge after the fine bubbles adsorbed by the dirt are electrically sucked by the plus electrode. 前記プラス電極は、ハニカム構造の電極部を有することを特徴とする請求項1〜3のいずれか1つに記載の浴水汚れ分解装置。   The bath water dirt decomposing apparatus according to any one of claims 1 to 3, wherein the positive electrode has an electrode portion having a honeycomb structure. 前記ハニカム構造の電極部を前記追焚き用の配管内で回転させる駆動部を更に有することを特徴とする請求項4に記載の浴水汚れ分解装置。   5. The bath water dirt decomposing apparatus according to claim 4, further comprising a drive unit configured to rotate the electrode portion of the honeycomb structure in the tracking pipe. 前記汚れが吸着した微小泡を前記プラス電極で電気的に吸引し、該プラス電極が回転した後に前記汚れを前記放電により分解すること特徴とする請求項4または5に記載の浴水汚れ分解装置。   6. The bath water dirt decomposing apparatus according to claim 4 or 5, wherein the dirt is adsorbed by the positive electrode, and the dirt is decomposed by the discharge after the plus electrode rotates. . 前記プラス電極および前記マイナス電極の各々はチタン製電極であるか、またはチタン製、ステンレス製、もしくはタングステン製の基材にプラチナ、銀、もしくは金をコーティングした電極であり、
該プラス電極と該マイナス電極との電極距離は20mm以下である、
ことを特徴とする請求項1〜6のいずれか1つに記載の浴水汚れ分解装置。
Each of the positive electrode and the negative electrode is a titanium electrode, or an electrode obtained by coating a substrate made of titanium, stainless steel, or tungsten with platinum, silver, or gold,
The electrode distance between the positive electrode and the negative electrode is 20 mm or less.
The bath water dirt decomposing apparatus according to any one of claims 1 to 6.
前記プラス電極および前記マイナス電極の各々は金属製、セラミックス製、または合成樹脂製の基材の表面に吸着剤および酸化触媒の少なくとも一方が添着された電極であることを特徴とする請求項1〜6のいずれか1つに記載の浴水汚れ分解装置。   Each of the positive electrode and the negative electrode is an electrode in which at least one of an adsorbent and an oxidation catalyst is attached to the surface of a base made of metal, ceramics, or synthetic resin. 6. The bath water dirt decomposing apparatus according to any one of 6 above. 前記酸化触媒は酸化チタンもしくは酸化マンガン、または該酸化チタンもしくは酸化マンガンの表面に貴金属を担持させたものであり、
前記吸着剤はゼオライトまたは活性炭である、
ことを特徴とする請求項8に記載の浴水汚れ分解装置。
The oxidation catalyst is titanium oxide or manganese oxide, or a noble metal supported on the surface of the titanium oxide or manganese oxide,
The adsorbent is zeolite or activated carbon;
The bath water dirt decomposing apparatus according to claim 8.
貯湯タンクに貯留した湯を熱源として用いる追焚き用熱交換器を備え、浴槽から取り出した浴水を前記追焚き用熱交換器により加熱した後に前記浴槽に戻す追焚き運転を行うことができる追焚き機能付き給湯機であって、
前記追焚き用の配管内に配置されるプラス電極およびマイナス電極と、前記プラス電極と前記マイナス電極とに電圧を印加して、該プラス電極と該マイナス電極との間に放電を生じさせる電源部とを備え、前記追焚き用の配管を流れる浴水中の汚れを前記放電により分解する浴水汚れ分解装置を具備したことを特徴とする追焚き機能付き給湯機。
A reheating heat exchanger that uses hot water stored in a hot water storage tank as a heat source is provided, and a reheating operation in which the bath water taken out from the bathtub is heated by the reheating heat exchanger and then returned to the bathtub can be performed. A water heater with a firewood function,
A positive electrode and a negative electrode disposed in the pursuit pipe, and a power supply unit that applies a voltage to the positive electrode and the negative electrode to generate a discharge between the positive electrode and the negative electrode And a bath water dirt decomposing device that decomposes the dirt in the bath water flowing through the chase pipe by the discharge.
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010179206A (en) * 2009-02-03 2010-08-19 Mitsubishi Electric Corp Purification device
JP2012020264A (en) * 2010-07-16 2012-02-02 Mitsubishi Electric Corp Water sterilization method, water sterilizing device, and air conditioner, hand dryer and humidifier using the water sterilizing device
JP2012127617A (en) * 2010-12-17 2012-07-05 Mitsubishi Electric Corp Water heater
JP2013139951A (en) * 2011-12-29 2013-07-18 Daikin Industries Ltd Hot water supply system
JP2013138982A (en) * 2011-12-29 2013-07-18 Daikin Industries Ltd Hot water supply system
CN103900259A (en) * 2014-03-04 2014-07-02 芜湖美的厨卫电器制造有限公司 Gas water heater with ultraviolet sterilization function and water storage type water heater with ultraviolet sterilization function
CN103900261A (en) * 2014-02-28 2014-07-02 芜湖美的厨卫电器制造有限公司 Water heater and method for controlling ultraviolet sterilization of water heater
JP2017508612A (en) * 2014-03-11 2017-03-30 ジェイピーエム エンジニアリング 株式会社 Wastewater purification system using high voltage discharge and fine foaming

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08173512A (en) * 1994-12-27 1996-07-09 Sharp Corp Deodorizing element
JPH09108676A (en) * 1995-10-17 1997-04-28 Rimoderingu Touenteiwan:Kk Method of purifying water and device therefor
JPH09206628A (en) * 1996-02-06 1997-08-12 Sharp Corp Apparatus for cleaning air
JP2001333966A (en) * 2000-05-26 2001-12-04 Matsushita Electric Works Ltd Air cleaner
JP2006284030A (en) * 2005-03-31 2006-10-19 Daikin Ind Ltd Bath device
JP2007021411A (en) * 2005-07-19 2007-02-01 Toshiba Kyaria Kk Electrostatic precipitator and air conditioner

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08173512A (en) * 1994-12-27 1996-07-09 Sharp Corp Deodorizing element
JPH09108676A (en) * 1995-10-17 1997-04-28 Rimoderingu Touenteiwan:Kk Method of purifying water and device therefor
JPH09206628A (en) * 1996-02-06 1997-08-12 Sharp Corp Apparatus for cleaning air
JP2001333966A (en) * 2000-05-26 2001-12-04 Matsushita Electric Works Ltd Air cleaner
JP2006284030A (en) * 2005-03-31 2006-10-19 Daikin Ind Ltd Bath device
JP2007021411A (en) * 2005-07-19 2007-02-01 Toshiba Kyaria Kk Electrostatic precipitator and air conditioner

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010179206A (en) * 2009-02-03 2010-08-19 Mitsubishi Electric Corp Purification device
JP2012020264A (en) * 2010-07-16 2012-02-02 Mitsubishi Electric Corp Water sterilization method, water sterilizing device, and air conditioner, hand dryer and humidifier using the water sterilizing device
JP2012127617A (en) * 2010-12-17 2012-07-05 Mitsubishi Electric Corp Water heater
JP2013139951A (en) * 2011-12-29 2013-07-18 Daikin Industries Ltd Hot water supply system
JP2013138982A (en) * 2011-12-29 2013-07-18 Daikin Industries Ltd Hot water supply system
CN103900261A (en) * 2014-02-28 2014-07-02 芜湖美的厨卫电器制造有限公司 Water heater and method for controlling ultraviolet sterilization of water heater
CN103900259A (en) * 2014-03-04 2014-07-02 芜湖美的厨卫电器制造有限公司 Gas water heater with ultraviolet sterilization function and water storage type water heater with ultraviolet sterilization function
JP2017508612A (en) * 2014-03-11 2017-03-30 ジェイピーエム エンジニアリング 株式会社 Wastewater purification system using high voltage discharge and fine foaming

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