JP2001208428A - Hot water supply bath device provided with purifying function - Google Patents
Hot water supply bath device provided with purifying functionInfo
- Publication number
- JP2001208428A JP2001208428A JP2000016726A JP2000016726A JP2001208428A JP 2001208428 A JP2001208428 A JP 2001208428A JP 2000016726 A JP2000016726 A JP 2000016726A JP 2000016726 A JP2000016726 A JP 2000016726A JP 2001208428 A JP2001208428 A JP 2001208428A
- Authority
- JP
- Japan
- Prior art keywords
- hot water
- circuit
- filtering means
- electrolysis
- filtering
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 165
- 238000001914 filtration Methods 0.000 claims abstract description 112
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 54
- 238000010438 heat treatment Methods 0.000 claims abstract description 20
- 230000004931 aggregating effect Effects 0.000 claims description 25
- 239000000126 substance Substances 0.000 claims description 22
- 238000007872 degassing Methods 0.000 claims description 20
- 229910052751 metal Inorganic materials 0.000 claims description 14
- 239000002184 metal Substances 0.000 claims description 14
- 238000011144 upstream manufacturing Methods 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 4
- 238000001514 detection method Methods 0.000 claims description 3
- 238000005189 flocculation Methods 0.000 claims 1
- 230000016615 flocculation Effects 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 26
- 230000009471 action Effects 0.000 abstract description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 28
- 230000015271 coagulation Effects 0.000 description 14
- 238000005345 coagulation Methods 0.000 description 14
- 238000011001 backwashing Methods 0.000 description 12
- 238000000746 purification Methods 0.000 description 8
- 229910052782 aluminium Inorganic materials 0.000 description 7
- 241000894006 Bacteria Species 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 230000002776 aggregation Effects 0.000 description 5
- 230000005484 gravity Effects 0.000 description 5
- 238000003303 reheating Methods 0.000 description 5
- 238000004220 aggregation Methods 0.000 description 4
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 4
- -1 aluminum ions Chemical class 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000010926 purge Methods 0.000 description 3
- 230000004044 response Effects 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 102100031083 Uteroglobin Human genes 0.000 description 1
- 108090000203 Uteroglobin Proteins 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 150000004677 hydrates Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Control For Baths (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、業務用あるいは家
庭用として風呂水を浄化する浄化機能付き給湯風呂装置
に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hot water supply bath apparatus having a purifying function for purifying bath water for business use or home use.
【0002】[0002]
【従来の技術】従来のこの種の濾過装置は図3に示すよ
うに、懸濁物質を含んだ水の懸濁物質を凝集し大型化す
る凝集手段と、大型化した懸濁物質を濾過する濾過手段
と、水の水温制御手段とを備え、水に含まれる懸濁物質
を短時間で濾過分離することで迅速且つ安定した濾過性
能を有するものがある(例えば、特開平8−11773
7号公報)。2. Description of the Related Art As shown in FIG. 3, a conventional filtering apparatus of this type aggregates a suspended substance containing water and aggregates the suspended substance, and filters the enlarged suspended substance. There is a filter provided with a filtration unit and a water temperature control unit, and has a quick and stable filtration performance by filtering and separating a suspended substance contained in water in a short time (for example, Japanese Patent Application Laid-Open No. H8-11773).
No. 7).
【0003】図において、1はポンプであり、浴槽2内
の湯を流路3で循環させている。4は流路3に設けられ
た水素イオン濃度調整手段である。5はアルミニウムイ
オンを溶出し、水中の懸濁物質を凝集させる凝集手段で
あり、流路3に設けれられている。6は凝集した懸濁物
質を濾過する濾過手段であり、内部に濾材7と、濾材支
持板8が備えられている。9は殺菌手段である紫外線ラ
ンプであり、10は加熱手段である電気ヒータである。
11は湯の流れを示す矢印である。In FIG. 1, reference numeral 1 denotes a pump which circulates hot water in a bathtub 2 through a flow path 3. Reference numeral 4 denotes a hydrogen ion concentration adjusting means provided in the flow path 3. Reference numeral 5 denotes an aggregating means for eluting aluminum ions and aggregating suspended substances in water, and is provided in the channel 3. Reference numeral 6 denotes a filtering means for filtering the aggregated suspended substance, and is provided with a filter medium 7 and a filter medium support plate 8 therein. Reference numeral 9 denotes an ultraviolet lamp serving as a sterilizing unit, and reference numeral 10 denotes an electric heater serving as a heating unit.
Reference numeral 11 denotes an arrow indicating the flow of hot water.
【0004】この装置において、電気ヒータ10によっ
て一定の温度に保たれた浴槽2内の水はポンプ1によっ
て流路3、水素イオン濃度調整手段4を通過し凝集手段
5に送り込まれる。このとき、凝集手段4ではアルミニ
ウムイオンが加えられ、水酸化アルミニウムが生成され
る。水酸化アルミニウムは電気的にプラスに帯電してお
り、湯中の電気的にマイナスに帯電した細菌や懸濁物質
と電気的に吸着がおこり、懸濁物質が大型化される。大
型化した懸濁物質は濾過手段6内部に充填された濾材7
で濾過され、紫外線ランプ9で殺菌されて浴槽2に戻さ
れる。In this apparatus, water in a bath 2 kept at a constant temperature by an electric heater 10 is sent by a pump 1 through a flow path 3 and a hydrogen ion concentration adjusting means 4 to a flocculating means 5. At this time, aluminum ions are added in the aggregation means 4, and aluminum hydroxide is generated. Aluminum hydroxide is electrically positively charged, and electrically adsorbs to electrically negatively charged bacteria and suspended substances in hot water, whereby the suspended substance is enlarged. The large-sized suspended substance is supplied to the filter medium 7 filled in the filtration means 6.
And sterilized by the ultraviolet lamp 9 and returned to the bathtub 2.
【0005】[0005]
【発明が解決しようとする課題】しかしながら上記のよ
うな水浄化装置の構成では、凝集手段の電気分解の際に
水素ガスや酸素ガスが生じ、凝集手段内に溜まる。凝集
手段内部には懸濁物質を凝集するための電極が内蔵され
ており、生じたガスにより凝集手段内の液面が下がり、
電極が液面下からガス層に露出することがある。However, in the configuration of the water purifying apparatus as described above, hydrogen gas and oxygen gas are generated during the electrolysis of the aggregating means and accumulate in the aggregating means. An electrode for coagulating the suspended substance is built in the coagulation means, and the generated gas lowers the liquid level in the coagulation means,
The electrode may be exposed to the gas layer from below the liquid level.
【0006】液面からガス層に露出した電極部分では電
気分解ができず、実質電気分解面積が減少し、電気分解
を定電流で行う場合は、必要電気分解電圧が上昇した
り、電気分解の電源電圧超えた場合は溶融金属の電解電
流値が減少し、凝集による浄化性能が低下するという課
題があった。これは、凝集手段を濾過手段内に内蔵する
場合でも同様のことが考えられる。[0006] Electrolysis cannot be performed at the electrode portion exposed from the liquid surface to the gas layer, and the electrolysis area is substantially reduced. When the electrolysis is performed at a constant current, the required electrolysis voltage increases or the electrolysis takes place. When the power supply voltage is exceeded, there is a problem that the electrolytic current value of the molten metal decreases and the purification performance due to coagulation decreases. The same can be considered for the case where the aggregating means is incorporated in the filtering means.
【0007】[0007]
【課題を解決するための手段】本発明は上記課題を解決
するため、浴水を循環する循環回路と、循環回路に設け
られた循環ポンプと、循環回路に設けれ溶融金属を電気
分解させることで金属水和物を生成し浴水に含まれる懸
濁物質を凝集させる凝集手段と、循環回路に設けられ凝
集した懸濁物質を物理的に濾過する濾過手段と、循環回
路に接続され濾過手段の上流側と下流側をバイパスする
バイパス回路と、濾過手段上部とバイパス回路を接続す
るサブバイパス回路と、循環回路に接続された給湯加熱
手段とからなり、凝集手段が濾過手段内部上側に設けら
れると共に、給湯加熱手段から供給する湯水を濾過手段
上部から注入する或いは循環ポンプを動作させ循環する
浴水を濾過手段上部から注入することで、電気分解時に
発生するガスを濾過手段上方からサブバイパス回路及び
バイパス回路を介して浴槽へ置換排出するようにしたも
のである。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a circulating circuit for circulating bath water, a circulating pump provided in the circulating circuit, and a method for electrolyzing molten metal provided in the circulating circuit. Aggregating means for producing a metal hydrate and aggregating suspended substances contained in the bath water, a filtering means provided in a circulation circuit for physically filtering the aggregated suspended substances, and a filtration means connected to the circulation circuit A bypass circuit that bypasses the upstream side and the downstream side of the filter, a sub-bypass circuit that connects the upper part of the filtering means and the bypass circuit, and a hot water supply heating means that is connected to the circulation circuit. At the same time, the gas generated during the electrolysis is filtered by injecting the hot water supplied from the hot water supply heating means from the upper part of the filtering means or by operating the circulation pump to inject the circulating bath water from the upper part of the filtering means. Is obtained so as to replace discharged into tub from the means upward through the sub-bypass circuit and bypass circuit.
【0008】上記発明によれば、給湯加熱手段から供給
された湯水或いは循環ポンプで循環された浴水が、濾過
手段上方から注水されると、濾過手段内では電気分解時
に発生したガスが、濾過手段上方からサブバイパス回
路、バイパス管に順に押し出され、さらに循環回路を経
て浴槽に排出される。According to the above invention, when the hot water supplied from the hot water supply heating means or the bath water circulated by the circulation pump is injected from above the filtering means, the gas generated during the electrolysis is filtered in the filtering means. It is extruded from above the means into the sub-bypass circuit and the bypass pipe in order, and further discharged into the bathtub through the circulation circuit.
【0009】つまり、凝集手段の電気分解量に応じて濾
過槽上方から注水することで、電極が液面から上昇する
ことなく安定して電気分解が継続できる。That is, by injecting water from above the filtration tank in accordance with the amount of electrolysis of the aggregating means, the electrolysis can be stably continued without the electrodes rising from the liquid level.
【0010】また、常時電極を液面下に浸漬することが
可能となり、電極の酸化皮膜付着が防止できる。In addition, the electrode can always be immersed below the liquid level, and the adhesion of an oxide film to the electrode can be prevented.
【0011】[0011]
【発明の実施の形態】本発明の請求項1に係る浄化機能
付き給湯風呂装置は、浴水を循環する循環回路と、循環
回路に設けられた循環ポンプと、循環回路に設けれ溶融
金属を電気分解させることで金属水和物を生成し浴水に
含まれる懸濁物質を凝集させる凝集手段と、循環回路に
設けられ凝集した懸濁物質を物理的に濾過する濾過手段
と、循環回路に接続され濾過手段の上流側と下流側をバ
イパスするバイパス回路と、濾過手段上部とバイパス回
路を接続するサブバイパス回路と、循環回路に接続され
た給湯加熱手段とからなり、凝集手段が濾過手段内部上
側に設けられると共に、給湯加熱手段から供給する湯水
を濾過手段上部から注入することで、電気分解時に発生
するガスを濾過手段上方からサブバイパス回路及びバイ
パス回路を介して浴槽へ置換排出するものである。BEST MODE FOR CARRYING OUT THE INVENTION A hot water supply bath with a purifying function according to claim 1 of the present invention comprises a circulation circuit for circulating bath water, a circulation pump provided in the circulation circuit, and a molten metal provided in the circulation circuit. Aggregating means for generating metal hydrates by electrolysis and aggregating suspended substances contained in bath water; filtering means for physically filtering the agglomerated suspended substances provided in the circulation circuit; A bypass circuit that is connected and bypasses the upstream and downstream sides of the filtration means, a sub-bypass circuit that connects the upper part of the filtration means and the bypass circuit, and a hot water supply heating means that is connected to the circulation circuit; In addition to being provided on the upper side, by injecting hot water supplied from the hot water supply heating means from the upper part of the filtering means, gas generated at the time of electrolysis is passed from above the filtering means through the sub-bypass circuit and the bypass circuit. It is intended to replace discharged to the tank.
【0012】そして、濾過手段上方から注水されると、
濾過手段内では電気分解時に発生するガスが比重差によ
り、濾過手段上方からサブバイパス回路、バイパス管に
順に押し出され、濾過手段内が湯水で満たされると共
に、発生ガスは循環回路を経て浴槽に排出される。Then, when water is injected from above the filtering means,
In the filtering means, the gas generated during the electrolysis is pushed out from the upper part of the filtering means to the sub-bypass circuit and the bypass pipe in order due to the difference in specific gravity. Is done.
【0013】つまり、凝集手段の電気分解量に応じて給
水手段で注水することで電極が液面からガス層に露出す
るのを防止でき、安定して電気分解が継続できる。よっ
て凝集効果が安定し、浄化性能が安定する。In other words, by injecting water with the water supply means according to the amount of electrolysis of the aggregating means, it is possible to prevent the electrodes from being exposed from the liquid surface to the gas layer, and the electrolysis can be stably continued. Therefore, the aggregation effect is stabilized, and the purification performance is stabilized.
【0014】本発明の請求項2に係る浄化機能付き給湯
風呂装置は、浴水を循環する循環回路と、循環回路に設
けられた循環ポンプと、循環回路に設けれ溶融金属を電
気分解させることで金属水和物を生成し浴水に含まれる
懸濁物質を凝集させる凝集手段と、循環回路に設けられ
凝集した懸濁物質を物理的に濾過する濾過手段と、循環
回路に接続され濾過手段の上流側と下流側をバイパスす
るバイパス回路と、濾過手段上部とバイパス回路を接続
するサブバイパス回路と、循環回路に接続された給湯加
熱手段とからなり、凝集手段が濾過手段内部上側に設け
られると共に、循環ポンプを動作させ浴水を濾過手段上
部から注入することで、電気分解時に発生するガスを濾
過手段上方からサブバイパス回路及びバイパス回路を介
して浴槽へ置換排出するようにしたものである。According to a second aspect of the present invention, there is provided a hot water supply bath apparatus having a purifying function, wherein a circulation circuit for circulating bath water, a circulation pump provided in the circulation circuit, and a molten metal provided in the circulation circuit for electrolyzing molten metal. Aggregating means for producing a metal hydrate and aggregating suspended substances contained in the bath water, a filtering means provided in a circulation circuit for physically filtering the aggregated suspended substances, and a filtration means connected to the circulation circuit A bypass circuit that bypasses the upstream side and the downstream side of the filter, a sub-bypass circuit that connects the upper part of the filtering means and the bypass circuit, and a hot water supply heating means that is connected to the circulation circuit. At the same time, the circulating pump is operated to inject bath water from the upper part of the filtering means, so that gas generated during electrolysis is replaced and discharged from above the filtering means to the bath tub via the sub-bypass circuit and the bypass circuit. It is obtained by way.
【0015】そして、循環ポンプにより循環された浴水
が濾過手段上方から注水されると、濾過手段内では電気
分解時の発生ガスが比重差により、濾過手段上方からサ
ブバイパス回路、バイパス管と順に押し出され、濾過手
段内が浴水で満たされると共に、発生ガスが循環回路を
経て浴槽に排出される。When the bath water circulated by the circulating pump is injected from above the filtering means, the gas generated during the electrolysis in the filtering means, due to the specific gravity difference, flows from above the filtering means to the sub-bypass circuit and the bypass pipe in order. The water is pushed out, the inside of the filtering means is filled with bath water, and the generated gas is discharged to the bath tub through the circulation circuit.
【0016】つまり、凝集手段の電気分解量に応じて給
水手段で注水することで電極が液面下からガス層に露出
するのを防止でき、安定して電気分解が継続できる。よ
って凝集効果が安定し、浄化性能が安定する。In other words, by injecting water with the water supply means according to the amount of electrolysis of the coagulation means, it is possible to prevent the electrodes from being exposed to the gas layer from below the liquid surface, and to stably continue electrolysis. Therefore, the aggregation effect is stabilized, and the purification performance is stabilized.
【0017】本発明の請求項3に係る浄化機能付き給湯
風呂装置は、凝集手段での電気分解時間が所定時間に達
すれば、濾過手段のガス抜き動作を行うようにしたもの
である。According to a third aspect of the present invention, in the hot water supply bath apparatus having a purifying function, when the electrolysis time in the aggregating means reaches a predetermined time, the degassing operation of the filtering means is performed.
【0018】そして、電気分解時間が所定時間行われる
と、電気分時間に応じたガスが発生し、濾過手段内部上
方に滞留するが、所定時間が経過すれば、自動的に濾過
手段上方から注水することで、電気分解時の発生ガスが
濾過手段上方に接続されたサブバイパス回路からバイパ
ス回路を経て浴槽に押し出されるようになる。よって、
電極が液面下からガス層に露出することがなく、安定し
て電気分解が継続される。When the electrolysis time is carried out for a predetermined time, a gas corresponding to the electric time is generated and stays in the upper part of the filtering means, but after a predetermined time, water is automatically injected from above the filtering means. By doing so, the gas generated during the electrolysis is pushed out of the sub-bypass circuit connected above the filtering means to the bathtub via the bypass circuit. Therefore,
Electrolysis is stably continued without the electrodes being exposed to the gas layer from below the liquid level.
【0019】本発明の請求項4に係る浄化機能付き給湯
風呂装置は、電気分解時の電圧もしくは電流を検知する
ことで発生ガス量を検知するガス検知手段を備えたもの
である。A hot water supply bath with a purifying function according to a fourth aspect of the present invention is provided with gas detecting means for detecting the amount of gas generated by detecting the voltage or current at the time of electrolysis.
【0020】そして、定電流回路を用いて電気分解を行
う場合は、電極が液面より上昇すると、電気分解に使用
可能な電極面積が減少し、電解電圧が上昇するようにな
る。また、定電圧回路を用いて電気分解を行う場合は、
電極が液面下よりガス層に露出すると、電気分解に使用
可能な電極面積が減少し、電解電流が減少するようにな
る。つまり、電解時の電圧もしくは電流の変化を検知す
ることで、電極が液面下よりガス層に露出した状態を検
知できる。When electrolysis is performed using a constant current circuit, when the electrode rises above the liquid level, the electrode area usable for electrolysis decreases, and the electrolysis voltage rises. When electrolysis is performed using a constant voltage circuit,
When the electrode is exposed to the gas layer from below the liquid level, the electrode area available for electrolysis is reduced, and the electrolytic current is reduced. That is, by detecting a change in voltage or current during electrolysis, it is possible to detect a state in which the electrode is exposed to the gas layer from below the liquid level.
【0021】電極が液面上に出たことを検知すればガス
抜き動作を行い、電極を確実に液面下に位置させること
で溶融金属溶解量を安定させることとなる。When it is detected that the electrode has risen above the liquid level, a gas venting operation is performed, and the amount of molten metal dissolved can be stabilized by reliably positioning the electrode below the liquid level.
【0022】[0022]
【実施例】以下、本発明の実施例を図面に基づいて説明
する。Embodiments of the present invention will be described below with reference to the drawings.
【0023】(実施例1)図1は、本発明の実施例1の
浄化機能付き給湯風呂装置である。(Embodiment 1) FIG. 1 shows a hot water supply bath apparatus having a purifying function according to Embodiment 1 of the present invention.
【0024】図1において、9は浴槽10内の水を循環
する強制循環手段である循環ポンプ、11は循環回路で
ある。12は循環回路11に設けられた濾過手段であ
り、円筒状筐体12aと、その内部に充填されたアルミ
ナを主成分とする比重が3〜4の粒状濾材12bと、粒
状濾材12bを支持する濾床12c、筐体12aの上
方、下方にそれぞれ設けた循環回路11を接続する上蓋
12d、下蓋12eとで構成されている。In FIG. 1, reference numeral 9 denotes a circulation pump which is a forced circulation means for circulating water in a bathtub 10, and reference numeral 11 denotes a circulation circuit. Reference numeral 12 denotes a filtering means provided in the circulation circuit 11, which supports a cylindrical casing 12a, a granular filter medium 12b mainly containing alumina, having a specific gravity of 3 to 4, and a granular filter medium 12b. It is composed of a filter bed 12c, an upper lid 12d and a lower lid 12e that connect circulation circuits 11 provided above and below the housing 12a, respectively.
【0025】13は電気分解により金属水和物を生成し
浴槽水に含まれる懸濁物質を凝集させる凝集手段であ
り、アルミニウムからなる陽極13aと、陽極13aに
対向して所定隙間を介して設けられたステンレス性の陰
極13bと、陽極13a及び陰極13b間に電圧を印可
し定電流を通電する電源13cとで構成されている。ま
た凝集手段13は陰極13bと筐体12aが所定隙間を
形成するように濾過手段12内上方に設けられている。
尚、陽極13aと、陰極13bと、筐体12aはそれぞ
れ円形断面を有し、同心円状に設けられている。Numeral 13 denotes an aggregating means for generating a metal hydrate by electrolysis and aggregating suspended substances contained in the bath water. The aggregating means 13 is provided with an anode 13a made of aluminum and a predetermined gap facing the anode 13a. And a power supply 13c for applying a voltage between the anode 13a and the cathode 13b and supplying a constant current. The aggregating means 13 is provided above the inside of the filtering means 12 so that the cathode 13b and the housing 12a form a predetermined gap.
The anode 13a, the cathode 13b, and the housing 12a each have a circular cross section and are provided concentrically.
【0026】14は循環回路11に設けられ循環する水
の保温・追焚き、浴槽10への注湯、濾過手段12の逆
洗時の湯及び、エアパージ時の水を供給する給湯加熱手
段であり、バーナー14aと、熱交換器14bと、注湯
二方弁14c、流量制御弁14d、逆止弁14e、注湯
温度を検出するサーミスタ14fを備えた給湯管14g
とで構成されている。尚、給湯管14gは循環ポンプ9
の吐出側の循環回路11に接続されている。Numeral 14 denotes a hot water supply heating means provided in the circulation circuit 11 for keeping and reheating the circulating water, pouring the water into the bathtub 10, supplying hot water at the time of back washing of the filtering means 12, and supplying water at the time of air purging. , A burner 14a, a heat exchanger 14b, a two-way pouring valve 14c, a flow control valve 14d, a check valve 14e, and a hot water supply pipe 14g including a thermistor 14f for detecting a pouring temperature.
It is composed of The hot water supply pipe 14g is connected to the circulation pump 9
Is connected to the circulation circuit 11 on the discharge side.
【0027】15は給湯管14gが循環回路11に接続
された位置と、循環ポンプ9の吐出側の間に設けられた
循環二方弁である。16、17はそれぞれ、循環二方弁
15と浴槽10の間の循環回路11に設けられた浴槽水
位を検出する水位センサ、浴槽10内の湯温を検出する
サーミスタである。Reference numeral 15 denotes a circulating two-way valve provided between the position where the hot water supply pipe 14g is connected to the circulation circuit 11 and the discharge side of the circulation pump 9. Reference numerals 16 and 17 denote a water level sensor provided in the circulation circuit 11 between the circulation two-way valve 15 and the bathtub 10 for detecting a bathtub water level, and a thermistor for detecting the temperature of hot water in the bathtub 10.
【0028】18は第一の流路切替弁(電動三方弁)で
あり、循環ポンプ9の往き側、濾過手段12の上方側、
バイパス管19に接続するように設けられている。20
は第二の流路切替弁(電動三方弁)であり、濾過手段1
2の下流側、浴槽10への往き側、バイパス管19に接
続されている。尚バイパス管19は第一の流路切替弁1
8、第二の流路切替弁20を切り替えて濾過手段12を
バイパス可能な循環回路が形成されると共に、濾過手段
12の下方側から濾過手段12及び浴槽10に給湯可能
なようになっている。Reference numeral 18 denotes a first flow path switching valve (electrically operated three-way valve), which is the outlet side of the circulation pump 9, the upper side of the filtration means 12,
It is provided so as to be connected to the bypass pipe 19. 20
Is a second flow path switching valve (electrically operated three-way valve),
2 is connected to the bypass pipe 19 on the downstream side of the bathtub 10. In addition, the bypass pipe 19 is the first flow path switching valve 1
8. A circulation circuit is formed which can switch the second flow path switching valve 20 to bypass the filtering means 12, and can supply hot water to the filtering means 12 and the bathtub 10 from below the filtering means 12. .
【0029】21は濾過手段12の上蓋12dとバイパ
ス管19を接続するサブバイパス管であり、濾過手段1
2上部からバイパス管19への一方向流れと成るように
逆止弁22が設けられている。Reference numeral 21 denotes a sub-bypass pipe connecting the upper lid 12d of the filtering means 12 and the bypass pipe 19;
A check valve 22 is provided so as to flow in one direction from the upper part 2 to the bypass pipe 19.
【0030】23は濾過手段12の上側と第二の流路切
替弁20の下流側とを接続する排水管であり、排水二方
弁24が設けられている。Reference numeral 23 denotes a drain pipe connecting the upper side of the filtering means 12 and the downstream side of the second flow path switching valve 20, and a drain two-way valve 24 is provided.
【0031】25は循環ポンプ9、第一の流路切替弁1
8、第二の流路切替弁20、循環二方弁15、排水二方
弁22、流量制御弁14d、注湯二方弁14c、バーナ
ー14aの動作、凝集手段13の電源13c、水位セン
サ16、サーミスタ14f、サーミスタ17等の動作を
司るコントローラであり、濾過、逆洗、湯張り、足し
湯、追焚き、保温、エアパージの動作を制御している。25 is a circulation pump 9, a first flow path switching valve 1
8, second flow path switching valve 20, circulation two-way valve 15, drainage two-way valve 22, flow control valve 14d, pouring two-way valve 14c, operation of burner 14a, power supply 13c of aggregating means 13, water level sensor 16 , The thermistor 14f, the thermistor 17 and the like, and controls the operations of filtration, backwashing, hot water filling, hot water, additional heating, heat retention, and air purging.
【0032】次に風呂全自動運転について、それぞれの
動作・作用を図1、図2を用いて説明する。Next, the operations and actions of the bath fully automatic operation will be described with reference to FIGS.
【0033】浴槽10の排水栓が閉められた状態で自動
風呂運転(足し湯、沸きあげ、追焚き動作を自動的に行
う運転)を行うと、濾過手段12内の空気を排出するエ
アパージ動作と濾過手段12の逆洗動作が、最初に連続
して行われる。When an automatic bath operation (operation for automatically performing hot water, boiling and reheating operations) is performed in a state where the drain plug of the bathtub 10 is closed, an air purge operation for discharging air from the filtering means 12 is performed. The backwashing operation of the filtering means 12 is first performed continuously.
【0034】つまり、コントローラ25の動作指示によ
り、循環二方弁15が閉に、第一の流路切替弁18がバ
イパス管19と給湯加熱手段14を連通した状態に、第
二の流路切替弁20がバイパス管19と濾過手段12を
連通した状態に、排水二方弁24が閉から開にそれぞれ
切り替えられる。That is, in response to an operation instruction from the controller 25, the circulation two-way valve 15 is closed, and the first flow path switching valve 18 is brought into a state in which the bypass pipe 19 and the hot water supply heating means 14 are communicated. The two-way drainage valve 24 is switched from closed to open, with the valve 20 communicating the bypass pipe 19 and the filtering means 12.
【0035】この状態になれば、注湯二方弁14cで約
1秒間開、数秒間閉となる動作が行なわれ、給湯管14
gを通過した水がバイパス管19を通過して濾過手段1
2の下方から流れこむ。流れ込んだ水は濾床12cを通
過し、粒状濾材12bで形成される濾材層を通過し始
め、濾過手段12内の水位が段階的に上昇し、濾過手段
12内が水で満たされる。In this state, the operation of opening the pouring two-way valve 14c for about one second and closing it for several seconds is performed.
g passed through the bypass pipe 19 and the filtration means 1
2 flows from below. The flowing water passes through the filter bed 12c and starts passing through the filter medium layer formed by the granular filter medium 12b, the water level in the filter means 12 rises gradually, and the inside of the filter means 12 is filled with water.
【0036】このようにすることで、粒状濾材12bで
形成される濾材層が比較的固まった状態の場合でも、間
欠的に水が流れこむことで濾材層に数回水圧による衝撃
が発生し、濾材層に水路が生じ粒状路材12b同士がバ
ラバラにされる。In this way, even if the filter medium layer formed of the granular filter medium 12b is in a relatively hardened state, the intermittent flow of water causes impact on the filter medium layer several times due to water pressure, A water path is formed in the filter medium layer, and the granular path materials 12b are separated.
【0037】また、粒状濾材31bが一時的に水流によ
り巻き上げられることがあっても、流れが停止状態にな
れば直ぐに自重で沈降する。また、粒状濾材12bで形
成される濾材層や濾床12c近傍に空気が残っており、
気泡となって上昇しても流れが間欠的であり、気泡と粒
状濾材12bが分離され、気泡のみが上方に浮き上がる
ようになる。Further, even if the particulate filter medium 31b may be temporarily wound up by the water flow, it will settle down by its own weight as soon as the flow stops. In addition, air remains near the filter medium layer formed by the granular filter medium 12b and the filter bed 12c,
Even if the bubbles rise as bubbles, the flow is intermittent, the bubbles are separated from the particulate filter medium 12b, and only the bubbles rise upward.
【0038】よって、粒状濾材12bが濾過手段12か
ら外部に排出されるには至らない。この動作中、濾過手
段12に流れこんだ水は、排水二方弁24を通過して排
水管23から外部に排出される。Therefore, the particulate filter medium 12b is not discharged from the filter means 12 to the outside. During this operation, the water flowing into the filtration means 12 passes through the drainage two-way valve 24 and is discharged to the outside from the drainage pipe 23.
【0039】その後、注湯二方弁14cの開閉動作回数
が所定回数になれば、注湯二方弁14cを開にし、流量
調整弁14dで給湯水量を所定値に、サーミスタ14
f、バーナー14aで水温を約50℃にそれぞれ調整し
て濾過手段12の逆洗動作に移る。Thereafter, when the number of opening / closing operations of the pouring two-way valve 14c reaches a predetermined number, the pouring two-way valve 14c is opened, and the amount of hot water is set to a predetermined value by the flow control valve 14d, and the thermistor 14 is turned on.
f, The water temperature is adjusted to about 50 ° C. by the burner 14a, and the process proceeds to the backwashing operation of the filtration means 12.
【0040】濾過手段は、濾過時に細菌などと同時に細
菌などの栄養分となる浴水中の汚れを補足するため、そ
の内部は細菌繁殖の好環境であり、濾過手段12を洗浄
しても、細菌をゼロにすることは困難であり、放置して
いる間に細菌増殖が進行することがある。また細菌が増
殖する課程で発生する代謝物も増加する。The filtration means is a favorable environment for bacteria to grow, because the filtration means supplements dirt in the bath water which becomes a nutrient such as bacteria at the same time as bacteria during filtration. It is difficult to achieve zero, and bacterial growth may progress during standing. Also, metabolites generated during the process of growing bacteria increase.
【0041】そこで、濾過手段12内部で増加した汚れ
が濾過手段12下方から浴槽10に戻されることがない
ように、予め濾過手段12内部が洗浄される。洗浄に用
いられた排水は排水管23から外部に排出される。Therefore, the inside of the filtering means 12 is washed beforehand so that the dirt increased inside the filtering means 12 is not returned to the bath 10 from below the filtering means 12. The wastewater used for washing is discharged to the outside through the drainpipe 23.
【0042】逆洗動作が所定時間を経過すれば、注湯二
方弁14cが閉になり、第一の流路切替弁18がバイパ
ス管19と循環ポンプ9を連通した状態に、第二の流路
切替弁20がバイパス管19と浴槽10を連通した状態
に、循環二方弁15が開の状態に切り替えられ、逆洗動
作が終了する。When a predetermined time has elapsed for the backwashing operation, the two-way pouring valve 14c is closed, and the second flow switching valve 18 is brought into a state in which the bypass pipe 19 and the circulation pump 9 are communicated with each other. The circulation two-way valve 15 is switched to the open state with the flow path switching valve 20 communicating the bypass pipe 19 and the bathtub 10, and the backwashing operation ends.
【0043】次に逆洗動作が終了すれば、湯張り動作に
移る。コントローラ23の動作指示により、第二の流路
切替弁20がバイパス管19と浴槽10を連通した状態
に、循環二方弁15が開から閉に、排水二方弁22が開
から閉に、それぞれ切り替えられる。その後、注湯二方
弁14cが開になると、バーナー14aが燃焼され、熱
交換器14bで加熱された湯が給湯管14gを流れ始め
る。Next, when the backwashing operation is completed, the operation proceeds to the filling operation. By the operation instruction of the controller 23, the circulation two-way valve 15 is changed from the open state to the closed state, the drainage two-way valve 22 is changed from the open state to the closed state, and the second flow path switching valve 20 communicates the bypass pipe 19 and the bathtub 10. Each can be switched. Thereafter, when the pouring two-way valve 14c is opened, the burner 14a is burned, and the hot water heated by the heat exchanger 14b starts flowing through the hot water supply pipe 14g.
【0044】その後、循環二方弁15、循環ポンプ9を
介した循環回路11と、第一の流路切替弁18、バイパ
ス管19、第二の流路切替弁20を介した循環回路11
の二方向から浴槽10に供給されるようになる。Thereafter, the circulation circuit 11 via the circulation two-way valve 15 and the circulation pump 9 and the circulation circuit 11 via the first passage switching valve 18, the bypass pipe 19 and the second passage switching valve 20.
Are supplied to the bathtub 10 from two directions.
【0045】尚、浴槽29内の水位、湯温を検知するに
は、注湯二方弁14cを閉とし、循環ポンプ9を動作さ
せることで、循環回路11内の空気を完全に浴槽に排出
した後に、循環ポンプ9を停止し、循環二方弁15を閉
にして、水位センサ17で浴槽10の水位を確認する。To detect the water level and hot water temperature in the bathtub 29, the two-way pouring valve 14c is closed and the circulating pump 9 is operated to completely discharge the air in the circulating circuit 11 into the bathtub. After that, the circulation pump 9 is stopped, the circulation two-way valve 15 is closed, and the water level in the bathtub 10 is checked by the water level sensor 17.
【0046】また水位確認後、設定水位に満たない場合
は再度湯張り動作を行ない、設定水位に達している場合
は、注湯二方弁14cを開とし、循環ポンプ9を動作さ
せ、循環回路11内を流れる湯の温度をサーミスタ16
で検知し水温を確認する。After the water level is confirmed, if the water level is lower than the set water level, the filling operation is performed again. The temperature of hot water flowing through the inside of the
To check the water temperature.
【0047】さらに水温確認後、設定水温に満たない場
合は循環ポンプ9を運転させながらバーナー14aを燃
焼させ、熱交換器14bで受熱して、浴槽10内の水を
追焚きするようになる。設定水温になれば、バーナー1
4aの燃焼、循環ポンプ9の運転が停止される。Further, after checking the water temperature, if the temperature is lower than the set water temperature, the burner 14a is burned while the circulation pump 9 is operated, the heat is received by the heat exchanger 14b, and the water in the bathtub 10 is additionally heated. When the set water temperature is reached, burner 1
The combustion of 4a and the operation of the circulation pump 9 are stopped.
【0048】湯張り動作が終了すれば、次に凝集動作、
ガス抜き動作、濾過動作が継続して行なわれる。凝集、
ガス抜き、濾過の動作・作用を図1、図2を用いて説明
する。When the filling operation is completed, the coagulation operation is performed next.
The degassing operation and the filtering operation are continuously performed. Agglomeration,
The operation and action of degassing and filtering will be described with reference to FIGS.
【0049】コントローラ25の動作指示により、排水
二方弁22が閉止、第一の流路切替弁18がバイパス管
19と給湯管14d側を連通した状態に、第二の流路切
替弁20が濾過手段12下方側を閉止した状態にそれぞ
れ切り替えられる。さらに電源13cがONされ、アル
ミニウムからなる陽極13aとステンレスからなる陰極
13b間に定電流が流れる様に制御され、所定時間t1
電気分解される。このようになれば、陽極13aからア
ルミニウムが溶解され水中にアルミニウムイオンが溶出
する。In response to an operation instruction from the controller 25, the drainage two-way valve 22 is closed, the first flow path switching valve 18 is in communication with the bypass pipe 19 and the hot water supply pipe 14d, and the second flow path switching valve 20 is turned on. The state is switched to a state in which the lower side of the filtering means 12 is closed. Further power 13c is ON, a constant current is controlled so as flowing between a cathode 13b made of an anode 13a and stainless made of aluminum, the predetermined time t 1
Electrolyzed. In this case, aluminum is dissolved from the anode 13a and aluminum ions are eluted in water.
【0050】このアルミニウムイオンは水中にある水酸
基(OH-)と化学反応して、電気的にプラスに帯電し
た水酸化アルミニウムとして水中に存在するようにな
る。この時、陽極13aからは水素H2が発生し、濾過
手段12の上方に溜まるようになる。This aluminum ion chemically reacts with a hydroxyl group (OH − ) in the water to be present in the water as aluminum hydroxide which is electrically positively charged. At this time, hydrogen H 2 is generated from the anode 13 a and accumulates above the filtering means 12.
【0051】この凝集動作の際は、循環二方弁15を閉
止し、水位センサ17で浴槽水位を検知すると共に、循
環二方弁15を開成し、循環ポンプ9で浴水を循環する
ことで浴槽温度を検知することが同時に行われている。In this coagulation operation, the circulation two-way valve 15 is closed, the water level sensor 17 detects the bathtub water level, the circulation two-way valve 15 is opened, and the circulation pump 9 circulates the bathwater. Sensing the bath tub temperature is being performed simultaneously.
【0052】この時、設定水位に満たない場合は足し湯
が、設定水温に満たない場合は追焚きが行われる。At this time, if the water level is lower than the set water level, the hot water is added. If the water temperature is lower than the set water temperature, additional heating is performed.
【0053】その後、電気分解時間が所定時間t1に達
すれば、ガス抜き動作に移る。この際、設定湯温になっ
ていない場合は循環ポンプを用いてガス抜きを行う様
に、設定水位になっていない場合は、給湯加熱手段を用
いて行う様に制御される。Thereafter, when the electrolysis time reaches a predetermined time t 1 , the operation shifts to a degassing operation. At this time, control is performed such that when the temperature of the hot water has not reached the set temperature, gas is released using a circulating pump.
【0054】まず設定水位以下の状態にあるときに、ガ
ス抜きを行う方法について説明する。コントローラ25
の動作指示により、循環二方弁が閉、排水二方弁24が
閉、第一の流路切替弁18が濾過手段12と給湯管14
d側を連通した状態に、第二の流路切替弁20が濾過手
段12下方側を閉止、バイパス管19と浴槽10を連通
した状態にそれぞれ切り替えられる。27は給湯加熱手
段14を用いてガス抜きを行う際の水の流れを示す実線
矢印である。First, a method for degassing when the water level is equal to or lower than the set water level will be described. Controller 25
, The circulation two-way valve is closed, the drainage two-way valve 24 is closed, and the first flow path switching valve 18 is connected to the filtration means 12 and the hot water supply pipe 14.
The second flow path switching valve 20 closes the lower side of the filtration means 12 and switches to a state where the bypass pipe 19 and the bathtub 10 communicate with each other so that the d side is communicated. Reference numeral 27 denotes a solid arrow indicating the flow of water when degassing is performed using the hot water supply heating unit 14.
【0055】また、流量調整弁14dはガス抜き動作に
必要な流量を流すようにその開成度が調整されると共
に、出湯温度が浴水保温温度となるようにバーナー14
aの燃焼量が調整される。尚、注湯二方弁14cは所定
時間t2だけ開成し、その後閉止する。The degree of opening of the flow control valve 14d is adjusted so that a flow necessary for the degassing operation flows, and the burner 14d is controlled so that the tap water temperature becomes the bath water keeping temperature.
The combustion amount of a is adjusted. Incidentally, pouring the two-way valve 14c is only open a predetermined time t 2, and then closed.
【0056】次に設定温度以下の状態にあるときに、ガ
ス抜きを行う方法について説明する。コントローラ25
の動作指示により、循環二方弁が開、排水二方弁24が
閉、第一の流路切替弁18が濾過手段12と給湯管14
d側を連通した状態に、第二の流路切替弁20が濾過手
段12下方側を閉止、バイパス管19と浴槽10を連通
した状態にそれぞれ切り替えられ、循環ポンプ9が運転
される。Next, a method of degassing when the temperature is equal to or lower than the set temperature will be described. Controller 25
, The circulation two-way valve is opened, the drainage two-way valve 24 is closed, and the first flow path switching valve 18 is connected to the filtering means 12 and the hot water supply pipe 14.
The second flow path switching valve 20 closes the lower side of the filtering means 12 in a state where the d side is communicated, and is switched to a state in which the bypass pipe 19 and the bathtub 10 are communicated, and the circulation pump 9 is operated.
【0057】尚、循環ポンプ9は所定時間t2だけ動作
し、その後停止する。また、バーナー14aの燃焼は所
定時間t2以内において浴水が所定温度に上昇した時点
で停止し、所定時間t2になれば、浴水温度に関わらず
停止する。28は循環ポンプ9を用いてガス抜きを行う
際の水の流れを示す破線矢印である。The circulating pump 9 operates for a predetermined time t 2 and then stops. The combustion of burners 14a is stopped when the bath water is increased to a predetermined temperature in within the predetermined time t 2, if the predetermined time t 2, and stops regardless bath water temperature. Reference numeral 28 is a broken line arrow indicating the flow of water when gas is released using the circulation pump 9.
【0058】さらに設定温度且つ設定水位の状態にある
ときは、バーナー14aを燃焼させずに、循環ポンプ9
を用いる方法でガス抜きを行う。When the temperature is at the set temperature and the set water level, the burner 14a is not burned and the circulating pump 9 is turned off.
Degassing is performed by a method using
【0059】上記したように、この様なガス抜き動作が
行われることで、給湯手段から供給された湯、或いは循
環ポンプ9で循環される浴水が濾過手段上方から注湯さ
れ、濾過手段上方から電気分解時に発生し滞留したガス
が比重差により濾過手段12上部に接続されたサブバイ
パス管21から排出され湯水と置換されるようになる。
さらに置換されたガスはバイパス管19から浴槽10に
排出される。As described above, by performing such a degassing operation, the hot water supplied from the hot water supply means or the bath water circulated by the circulation pump 9 is poured from above the filtration means, and is supplied from above the filtration means. The gas generated and retained during the electrolysis is discharged from the sub-bypass pipe 21 connected to the upper part of the filtering means 12 due to the difference in specific gravity and is replaced with hot water.
Further, the replaced gas is discharged from the bypass pipe 19 to the bathtub 10.
【0060】この動作が行われることで、濾過手段12
内は再度湯水で満たされると共に、浴槽温度、浴槽水位
が設定状態に近づくこととなる。By performing this operation, the filtering means 12
The inside is filled with hot water again, and the bathtub temperature and the bathtub water level approach the set states.
【0061】次に濾過時の動作・作用を説明する。コン
トローラ25の動作指示により、排水二方弁24が閉
止、循環二方弁15が開成、第一の流路切替弁18が濾
過手段12と循環ポンプ9側を連通した状態に、第二の
流路切替弁20が濾過手段12と浴槽10を連通した状
態にそれぞれ切り替えられ、循環ポンプ9が運転され
る。Next, the operation and operation at the time of filtration will be described. In response to an operation instruction from the controller 25, the drainage two-way valve 24 is closed, the circulation two-way valve 15 is opened, and the first flow path switching valve 18 is connected to the filtration means 12 and the circulation pump 9 side. The path switching valve 20 is switched to a state in which the filtration means 12 and the bathtub 10 are communicated, and the circulation pump 9 is operated.
【0062】このようになれば、濾過手段12内に浴槽
10から浴水中に含まれる垢や細菌といった電気的にマ
イナスに帯電した懸濁物質が流入する。In this case, suspended substances electrically negatively charged such as dirt and bacteria contained in the bath water flow from the bathtub 10 into the filtering means 12.
【0063】濾過手段12内には電気分解により生成さ
れた電気的にプラスに帯電した水酸化アルミニウムが滞
留しており、懸濁物質が流入することで濾過手段12内
で混合撹拌され、電気的に中和された懸濁物質の凝集フ
ロックが形成されるようになる。発明者等は、この凝集
フロックの粒子径が数十から数百μmになることを確認
している。The positively charged aluminum hydroxide generated by the electrolysis stays in the filtration means 12 and is mixed and agitated in the filtration means 12 by the inflow of the suspended matter, and Agglomerated flocs of the neutralized suspended matter are formed. The inventors have confirmed that the particle size of the aggregated floc is several tens to several hundreds μm.
【0064】このようになれば濾過手段12に充填され
た粒子径が0.3〜0.5mmの粒状濾材12bで構成さ
れる濾材層で、凝集フロックが濾過分離される。つま
り、浴水に含まれる懸濁物質が除去され浴槽10に戻さ
れる。In this way, the flocculated floc is separated by filtration in the filter medium layer composed of the particulate filter medium 12b having a particle diameter of 0.3 to 0.5 mm filled in the filter means 12. That is, the suspended matter contained in the bath water is removed and returned to the bathtub 10.
【0065】この濾過動作が所定時間t3だけ行われれ
ば、凝集動作に戻る。When the filtering operation is performed for a predetermined time t 3 , the operation returns to the aggregation operation.
【0066】また、ガス抜き動作は、所定時間t1だけ
電気分解されれば、自動的に移行するように制御されて
いるが、万一空気が溜まったり、ガス抜きが上手く行か
ずに、陽極13a及び陰極13bが液面から上昇する
と、電源13cでの電解電圧が上昇する。このように成
れば、コントローラ25に内蔵したガス発生検知手段2
6により電気分解が停止され、ガス抜き動作を行い、確
実に液面下に浸漬させるようになる。The degassing operation is controlled so as to automatically shift when electrolysis is performed for a predetermined time t 1. However, if air is accumulated or degassing does not go well, the anode degassing operation is stopped. When the cathode 13a and the cathode 13b rise from the liquid level, the electrolysis voltage at the power supply 13c rises. With this configuration, the gas generation detecting means 2 built in the controller 25
The electrolysis is stopped by 6 to perform a degassing operation, so that the liquid is reliably immersed below the liquid level.
【0067】さらに凝集動作は、総電解時間がt4を経
過すれば、凝集動作は終了し電気分解を行わないよう
に、湯張り終了後所定時間t5経過すれば、保温・足し
湯、濾過運転が終了するように制御されている。Further, the coagulation operation is performed such that the coagulation operation is completed and the electrolysis is not performed if the total electrolysis time has elapsed t 4, and if the predetermined time t 5 has elapsed after completion of the filling, the heat retention / addition hot water and filtration are performed. The operation is controlled to end.
【0068】尚、給湯風呂装置の電源が入った状態で且
つ全自動運転が解除された状態では、追焚き・足し湯動
作は行わないようにしている。When the power of the hot water supply bath is turned on and the fully automatic operation is released, the reheating and adding hot water operation is not performed.
【0069】また濾過動作が継続されると、濾過運転後
の濾過手段12内部の粒状濾材12bで形成される濾材
層の上層から中層にかけては、凝集フロック等の汚れが
堆積しており、濾過手段12内を洗浄するため逆洗動作
を行う必要が生じる。When the filtration operation is continued, dirt such as flocculated floc is accumulated from the upper layer to the middle layer of the filter medium layer formed by the particulate filter medium 12b inside the filter means 12 after the filtration operation. It is necessary to perform a backwashing operation to wash the inside of the cleaning device 12.
【0070】逆洗動作は、湯張り終了から所定時間t6
が経過すれば、自動的に行うように制御されている。逆
洗動作は前述した通りであり、省略する。The backwashing operation is performed for a predetermined time t 6 from the end of the hot water filling.
Is controlled so that it is automatically performed when the time elapses. The backwashing operation is as described above, and is omitted.
【0071】以上、本実施例では以下に示す効果があ
る。As described above, this embodiment has the following effects.
【0072】集動作開始時に、浴水の水位検知及び湯温
チェックを行なうと共に、追焚き、足し湯を行う全自動
運転を行うことで、限られた時間内で最大限濾過時間に
あてることができる。よって、浄化性能が向上する。At the start of the collecting operation, the water level of the bath water is detected and the temperature of the hot water is checked, and the fully automatic operation of reheating and adding hot water is performed, so that the maximum filtering time can be reached within a limited time. it can. Therefore, the purification performance is improved.
【0073】凝集動作時に水位及び湯温検知結果に基づ
き、ガス抜き時に、足し湯、追焚き動作を行うことがで
きる。Based on the water level and hot water temperature detection results during the coagulation operation, the hot water and additional heating operations can be performed at the time of degassing.
【0074】湯張り時に先立ち逆洗動作を行うことで、
濾過手段逆洗後放置に伴う濾過手段内の細菌増殖による
汚れが、浴槽に戻ることを防ぐことができる。By performing a backwash operation prior to filling with hot water,
It is possible to prevent the contamination due to the bacterial growth in the filtration means accompanying the standing after the filtration means backwashing from returning to the bathtub.
【0075】粒状濾材を比重の大きいアルミナで構成す
ることにより、粒状濾材の流出を減少させることができ
ると共に、比較的粒状濾材の粒径を小さくできるため濾
過性能を向上させることができる。When the granular filter medium is composed of alumina having a large specific gravity, the outflow of the granular filter medium can be reduced, and the particle size of the granular filter medium can be made relatively small, so that the filtering performance can be improved.
【0076】濾過手段に給湯加熱部からの温水を供給す
ることで、濾過手段の洗浄効率が向上する。By supplying hot water from the hot water supply heating unit to the filtering means, the washing efficiency of the filtering means is improved.
【0077】[0077]
【発明の効果】以上の説明から明らかのように、本発明
によれば、次の効果が得られる。As is clear from the above description, according to the present invention, the following effects can be obtained.
【0078】本発明の請求項1に係る浄化機能付き給湯
風呂装置は、濾過手段上方から注水することで、電気分
解時の発生ガスを置換排出し、電極が液面から上に出る
のを防止できる。よって、電気分解が安定し、確実に凝
集効果が得られ浄化性能が確保できる。また、ガス抜き
動作と同時に浴水の水位検知や給湯加熱手段で浴水の足
し湯動作も可能である。In the hot-water supply bath apparatus with a purifying function according to the first aspect of the present invention, the gas generated during the electrolysis is replaced and discharged by pouring water from above the filtering means, and the electrode is prevented from coming out of the liquid surface. it can. Therefore, the electrolysis is stable, the coagulation effect is reliably obtained, and the purification performance can be secured. Also, at the same time as the degassing operation, the level of the bath water can be detected and the operation of adding hot water can be performed by hot water supply heating means.
【0079】また、本発明の請求項2に係る浄化機能付
き給湯風呂装置は、循環ポンプで循環する浴水を濾過手
段上方から注水することで、電気分解時の発生ガスを置
換排出し、電極が液面から上に出るのを防止できる。よ
って、電気分解が安定し、確実に凝集効果が得られ浄化
性能が確保できる。また、浴槽水位を変動させることな
くガス抜き動作が行えるとともに、ガス抜き時に浴水の
追焚き動作も可能となる。Further, in the hot water supply bath apparatus with a purifying function according to claim 2 of the present invention, the bath water circulated by the circulating pump is injected from above the filtering means, thereby replacing and discharging the gas generated during the electrolysis, and Can be prevented from rising above the liquid level. Therefore, the electrolysis is stable, the coagulation effect is reliably obtained, and the purification performance can be secured. Further, the degassing operation can be performed without changing the bathtub water level, and the reheating operation of the bathwater can be performed at the time of degassing.
【0080】また、本発明の請求項3に係る浄化機能付
き給湯風呂装置は、電気分解動作が所定時間経過すれ
ば、自動的に濾過手段上方から注水することで、濾過手
段上方から電気分解時の発生ガスを置換排出することが
できる。つまり電極を液面下に浸漬した状態を維持する
ことができ、電気分解による凝集作用を安定させること
が可能となる。Further, in the hot water bath apparatus with a purifying function according to claim 3 of the present invention, the water is automatically injected from above the filter means when the electrolysis operation has passed for a predetermined time, so that the electrolyzer is operated from above the filter means. Can be replaced and discharged. That is, it is possible to maintain a state in which the electrode is immersed below the liquid surface, and it is possible to stabilize the coagulation action by electrolysis.
【0081】また、本発明の請求項4に係る浄化機能付
き給湯風呂装置は、電解時の電圧変化を検知すること
で、電極と液面の位置関係を把握することが可能とな
る。万一、液面より上昇する状態となっても、ガス抜き
動作を行うことで確実に液面下に浸漬させることがで
き、電気分解による凝集作用を安定させることが可能と
なる。Further, the hot water supply bath apparatus with a purifying function according to the fourth aspect of the present invention can grasp the positional relationship between the electrode and the liquid level by detecting a voltage change during electrolysis. Even if the liquid level rises above the liquid level, it is possible to ensure that the liquid is immersed beneath the liquid level by performing the degassing operation, thereby stabilizing the coagulation action by electrolysis.
【図1】本発明の実施例1における浄化機能付き給湯風
呂装置の模式構成図FIG. 1 is a schematic configuration diagram of a hot water supply bath apparatus with a purification function according to a first embodiment of the present invention.
【図2】同装置の湯張り動作から逆洗動作までの状態を
表すシーケンス図FIG. 2 is a sequence diagram showing a state from a hot water filling operation to a backwashing operation of the apparatus.
【図3】従来の水浄化装置の模式構成図FIG. 3 is a schematic configuration diagram of a conventional water purification device.
9 循環ポンプ 11 循環回路 12 濾過手段 12b 粒状濾材 13 凝集手段 13a 陽極 13b 陰極 13c 電源 14 給湯加熱手段 15 循環二方弁 18 第一の流路切替弁(電動三方弁) 19 バイパス管 20 第二の流路切替弁(電動三方弁) 21 サブバイパス管 26 ガス発生検知手段 Reference Signs List 9 circulation pump 11 circulation circuit 12 filtration means 12b granular filter medium 13 coagulation means 13a anode 13b cathode 13c power supply 14 hot water supply heating means 15 circulation two-way valve 18 first flow path switching valve (electric three-way valve) 19 bypass pipe 20 second Flow path switching valve (electrically operated three-way valve) 21 Sub-bypass pipe 26 Gas generation detection means
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 3L024 CC02 CC10 DD02 DD17 DD19 DD21 DD27 DD32 GG05 GG06 GG07 GG12 GG38 GG41 HH13 HH26 HH42 HH45 4D061 DA07 DB15 EA06 EB27 EB28 EB37 EB39 FA01 FA13 FA20 GA04 GA09 GA12 GA14 GA30 GC04 GC15 GC20 4D064 AA11 BF32 BF33 BF34 BF36 BF40 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 3L024 CC02 CC10 DD02 DD17 DD19 DD21 DD27 DD32 GG05 GG06 GG07 GG12 GG38 GG41 HH13 HH26 HH42 HH45 4D061 DA07 DB15 EA06 EB27 EB28 EB37 EB39 FA01 FA13 FA20 GA04 GA09 GC04 4D064 AA11 BF32 BF33 BF34 BF36 BF40
Claims (4)
に設けられた循環ポンプと、前記循環回路に設けた溶融
金属を電気分解して金属水和物を生成させ浴水に含まれ
る懸濁物質を凝集する凝集手段と、前記懸濁物質を物理
的に濾過する濾過手段と、前記循環回路に接続され前記
濾過手段の上流側と下流側をバイパスするバイパス回路
と、前記濾過手段上部と前記バイパス回路を接続するサ
ブバイパス回路と、前記循環回路に接続された給湯加熱
手段とからなり、前記凝集手段を前記濾過手段の内部上
側に設けると共に、前記給湯加熱手段から供給する湯水
を前記濾過手段上部から注入することにより、電気分解
時に発生するガスを前記濾過手段上方から前記サブバイ
パス回路及び前記バイパス回路を介して浴槽へ置換排出
する浄化機能付き給湯風呂装置。A circulating circuit for circulating bath water, a circulating pump provided in the circulating circuit, and a metal hydrate formed by electrolyzing molten metal provided in the circulating circuit and contained in the bath water. An aggregating means for aggregating the suspended substance, a filtering means for physically filtering the suspended substance, a bypass circuit connected to the circulation circuit and bypassing the upstream and downstream sides of the filtering means, and an upper part of the filtering means And a sub-bypass circuit connecting the bypass circuit, and hot water supply heating means connected to the circulation circuit, wherein the aggregating means is provided on the upper inside of the filtration means, and the hot water supplied from the hot water supply heating means is With a purifying function for injecting gas generated during electrolysis from the upper part of the filtering means and replacing and discharging the gas generated from the upper part of the filtering means to the bathtub through the sub-bypass circuit and the bypass circuit. Hot water bath equipment.
に設けられた循環ポンプと、前記循環回路に設けた溶融
金属を電気分解して金属水和物を生成させ浴水に含まれ
る懸濁物質を凝集する凝集手段と、前記懸濁物質を物理
的に濾過する濾過手段と、前記循環回路に接続され前記
濾過手段の上流側と下流側をバイパスするバイパス回路
と、前記濾過手段上部と前記バイパス回路を接続するサ
ブバイパス回路と、前記循環回路に接続された給湯加熱
手段とからなり、前記凝集手段を前記濾過手段の内部上
側に設けると共に、前記循環ポンプを動作させ浴水を前
記濾過手段の上部から注入することにより、電気分解時
に発生するガスを前記濾過手段の上方から前記サブバイ
パス回路及び前記バイパス回路を介して浴槽へ置換排出
する浄化機能付き給湯風呂装置。2. A circulating circuit for circulating bath water, a circulating pump provided in the circulating circuit, and a metal hydrate formed by electrolyzing molten metal provided in the circulating circuit and contained in the bath water. An aggregating means for aggregating the suspended substance, a filtering means for physically filtering the suspended substance, a bypass circuit connected to the circulation circuit and bypassing the upstream and downstream sides of the filtering means, and an upper part of the filtering means And a sub-bypass circuit connecting the bypass circuit, and a hot water supply heating means connected to the circulation circuit.The flocculation means is provided inside the filtration means, and the circulation pump is operated to supply bath water. With a purifying function of injecting gas generated at the time of electrolysis by injecting from the upper part of the filtering means, and replacing and discharging the gas generated from the electrolysis means from above the filtering means to the bathtub through the sub bypass circuit and the bypass circuit. Hot water bath equipment.
すれば、濾過手段のガス抜き動作を行う請求項1または
2記載の浄化機能付き給湯風呂装置。3. The hot-water supply bath with a purifying function according to claim 1, wherein the degassing operation of the filtering means is performed when the electrolysis time in the aggregating means reaches a predetermined time.
とにより発生ガス量を検知するガス検知手段を備えた請
求項1または2記載の浄化機能付き給湯風呂装置。4. The hot-water supply bath with a purifying function according to claim 1, further comprising gas detection means for detecting a generated gas amount by detecting a voltage or a current at the time of electrolysis.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000016726A JP2001208428A (en) | 2000-01-26 | 2000-01-26 | Hot water supply bath device provided with purifying function |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000016726A JP2001208428A (en) | 2000-01-26 | 2000-01-26 | Hot water supply bath device provided with purifying function |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001208428A true JP2001208428A (en) | 2001-08-03 |
Family
ID=18543819
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2000016726A Pending JP2001208428A (en) | 2000-01-26 | 2000-01-26 | Hot water supply bath device provided with purifying function |
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Country | Link |
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JP (1) | JP2001208428A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2440139A (en) * | 2006-07-20 | 2008-01-23 | John Bostock | Electrocoagulation unit for the removal of contaminants from a fluid |
KR101229559B1 (en) | 2010-12-30 | 2013-02-05 | 박철균 | Apparatus for controlling of bubble manufacturing in bathtub and method thereof |
CN114963506A (en) * | 2021-04-26 | 2022-08-30 | 青岛经济技术开发区海尔热水器有限公司 | Microbubble water heater |
-
2000
- 2000-01-26 JP JP2000016726A patent/JP2001208428A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2440139A (en) * | 2006-07-20 | 2008-01-23 | John Bostock | Electrocoagulation unit for the removal of contaminants from a fluid |
KR101229559B1 (en) | 2010-12-30 | 2013-02-05 | 박철균 | Apparatus for controlling of bubble manufacturing in bathtub and method thereof |
CN114963506A (en) * | 2021-04-26 | 2022-08-30 | 青岛经济技术开发区海尔热水器有限公司 | Microbubble water heater |
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