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JP3775017B2 - Circulating warm bath and electrode cleaning method - Google Patents
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JP3775017B2 - Circulating warm bath and electrode cleaning method - Google Patents

Circulating warm bath and electrode cleaning method Download PDF

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Publication number
JP3775017B2
JP3775017B2 JP27682697A JP27682697A JP3775017B2 JP 3775017 B2 JP3775017 B2 JP 3775017B2 JP 27682697 A JP27682697 A JP 27682697A JP 27682697 A JP27682697 A JP 27682697A JP 3775017 B2 JP3775017 B2 JP 3775017B2
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Japan
Prior art keywords
electrode
bath
aluminum
circulating
filtration tank
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JP27682697A
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JPH11114573A (en
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孝典 北川
真二 末松
光幸 中園
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Panasonic Corp
Panasonic Holdings Corp
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Panasonic Corp
Matsushita Electric Industrial Co Ltd
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  • Filtration Of Liquid (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、アルミニウム電解による凝集処理(浄化)と加熱保温の機能を備え、風呂の浴槽水を循環して再利用する循環温浴器及び電極洗浄方法に関するものである。
【0002】
【従来の技術】
近年、一旦使用された風呂の浴槽水を、循環ポンプを用いてプレフィルター(ヘアーキャッチャー)、ろ過槽、活性化タンク、保温用ヒータ等に循環させ、浴槽水の汚れの除去、活性化、加熱保温を行なう循環温浴器が一般家庭の風呂においても使用されるようになった。
【0003】
現在、市場における循環温浴器としては、生物処理を用いて浴槽水の浄化、脱臭を行なっているものがほとんどであるが、アルミニウム電解による凝集処理を行うものも注目されてきている。又、浴槽水の汚れの除去の他に悪臭や大腸菌、レジオネラ属菌、緑膿菌等の発生を防止する必要があるため、紫外線殺菌装置による殺菌処理を行うものや、小型のオゾン発生装置を設けてオゾン処理を行うものや、銀系の抗菌剤による殺菌処理を行うもの、更には浴槽水を電気分解する電解槽を備えて酸性水を浴槽水に戻す処理を行うもの等が開発されている。
【0004】
以下、アルミニウム電解による従来の循環温浴器について、図面を用いて説明する。
【0005】
図7は従来の循環温浴器のシステム概略図である。
図中、1は浴槽、2は浴槽水、3は浴槽1内に配設されたノズルユニット、4はノズルユニット3内へ浴槽水2が給水される給水口、5は給水口4から給水された浴槽水2の逆流を防止する逆止弁、6はスポンジ、ポリプロピレン等の樹脂製のメッシュ網、糸巻フィルター等からなるプレフィルター(ヘアーキャッチャー)、7は循環パイプ8を介してノズルユニット3と接続された従来の循環温浴器本体、9は循環パイプ8に配設されノズルユニット3からの浴槽水2の流量を検知する流量センサー、10は温度センサー、11は循環温浴器本体7の循環ポンプ、12は紫外線又はオゾン等を利用して循環ポンプ11から送出された浴槽水2を殺菌,脱臭する殺菌装置、13は循環ポンプ11と殺菌装置12を接続した循環パイプ、14はろ過槽、15a,15bは殺菌装置12とろ過槽14を接続した循環パイプ、16は循環パイプ15a,15bの連結点に配設された三方弁、17はろ過槽14の加熱殺菌用及び保温用のヒータ、17aはろ過槽14の温度センサー、18はろ過槽14内に配設されたアルミニウム電極、19はろ過槽14に配設されたSUS電極、20はろ過槽14内に配設されたガラスビーズ、セラミックボール、アルミナ等の砂等からなるろ材、21は循環温浴器本体7内を循環した浴槽水2を浴槽1に戻すジェットノズル、22a,22b,22cは循環温浴器本体7とジェットノズル21を接続した循環パイプ、23は循環パイプ22a,22bの連結点に配設された三方弁、24は循環パイプ22b,22cの連結点に配設された三方弁、25は循環温浴器本体7を洗浄した洗浄水を排水する逆洗排水口、26は三方弁16と逆洗排水口25を接続した逆洗パイプ、27は三方弁23と循環パイプ13を接続した逆洗パイプ、28は三方弁24と循環パイプ8を接続した循環パイプ、29は循環温浴器本体7の電源部、30は循環温浴器本体7の制御部、31は循環温浴器本体7の表示及び操作部である。
【0006】
以下、以上のように構成された従来の循環温浴器の動作について、図面を用いて説明する。
【0007】
図8は循環温浴器の通常循環時の浴槽水の流れを示した図であり、図9は循環温浴器ろ過槽の殺菌時を示した図であり、図10は循環温浴器の加熱殺菌循環時の浴槽水の流れを示した図であり、図11は循環温浴器の逆洗時の浴槽水の流れを示した図である。
【0008】
まず、循環温浴器の通常循環時について、図8を用いて説明する。
制御部30により通常循環動作が開始されると、三方弁16がa→c方向、三方弁23,24がc→a方向に切り替えられる。次に、循環ポンプ11が駆動して浴槽1内の浴槽水2がノズルユニット3の給水口4より吸い上げられ、プレフィルター6を通るとともにプレフィルター6により浴槽水2中に含まれる髪の毛等の大きなゴミが捕集され、更に、循環パイプ8を介し流量センサー9、温度センサー10を通り循環ポンプ11に流入する。
【0009】
ここで、循環流量の低下を防ぐために、プレフィルター6(特にスポンジ等からなる場合)を1,2週間に1回程度定期的に取り出し、付着している髪の毛等の大きなゴミを除去している。また、糸巻フィルターからなるプレフィルター6の場合、浴槽水2の循環流量がある一定の流量より低下した際に制御部30によって検知して表示及び操作部31によってプレフィルター6の洗浄又は交換時期を表示している。
【0010】
次に、循環ポンプ11から送出された浴槽水2は、紫外線またはオゾン等を利用した殺菌装置12により殺菌、脱臭されて三方弁16を介してろ過槽14へ流入する。
【0011】
ろ過槽14内において、アルミニウム電極18を陽極、SUS電極19を陰極として両電極間に電流を流して浴槽水2のアルミニウム電解を行い、浴槽水2中に水酸化アルミニウムを溶出し、この水酸化アルミニウムで浴槽水2中の懸濁成分である小さいゴミ、垢(無機物、蛋白及び脂質等の有機物)等を凝集させる。次に、ろ過槽14内のガラスビーズやセラミックボール、アルミナ等の砂等からなるろ材20によりプレフィルター6で取れなかった小さいゴミ、垢(無機物、蛋白及び脂質等の有機物)等の凝集物がろ過される(一般的にこれまでの流れを浄化と呼ぶ)。尚、浴槽水2はろ過槽14の加熱殺菌用及び保温用のヒータ17と温度センサー17aにより温度コントロールされている。
【0012】
ろ過槽14で浄化された浴槽水2は、三方弁23,24を介してジェットノズル21から浴槽1へ戻される。
【0013】
次に、循環温浴器ろ過槽14の殺菌時について、図9を用いて説明する。
制御部30により循環温浴器ろ過槽14の殺菌が開始されると、三方弁23がc→b方向に切り替えられるとともに、循環ポンプ11が停止して浴槽水2の循環が停止する。
【0014】
次に、ろ過槽14のヒータ17によりろ過槽14内の浴槽水2が温度70℃〜85℃まで加熱され、ろ過槽14内のレジオネラ属菌、緑膿菌等の殺菌が行われる。電極の洗浄は、必要に応じてクエン酸や酢酸、リンゴ酸等を浴槽水2に入れて循環運転してスケールをとるか、電極を取り出して手洗浄するかされる。
【0015】
次に、循環温浴器の加熱殺菌循環時について、図10を用いて説明する。
制御部30により加熱殺菌循環動作が開始されると、三方弁23がc→a方向、三方弁24がc→bに切り替えられるとともに、循環ポンプ11が作動し、図10に示すように、閉回路の循環系が形成される。
【0016】
温度70℃〜85℃まで加熱されたろ過槽14内の浴槽水2が三方弁23,24を介して循環ポンプ11、殺菌装置12を経てろ過槽14に再び戻り、閉回路の循環系内で循環してろ過槽14内及び循環パイプ8,13,15a,15b,22a,22b,28内のレジオネラ属菌、大腸菌、緑膿菌等を加熱殺菌する。
【0017】
次に、循環温浴器の逆洗時について、図11を用いて説明する。
制御部30により逆洗動作が開始されると、三方弁23がb→c方向、三方弁16がc→bに切り替えられる。
【0018】
循環ポンプ11により、給水口4から給水された浴槽水2が流量センサー9、温度センサー10が配設された循環パイプ8から逆洗パイプ27,三方弁23,循環パイプ22aを介してろ過槽14へ流入する。
【0019】
循環パイプ22aからろ過槽14内へ流入した浴槽水2は、ろ過槽14内のろ材20に付着,蓄積したゴミや汚れ及びアルミニウム凝集物等とともに循環パイプ15b,三方弁16,逆洗パイプ26を介して排水口25から排水される。
【0020】
尚、逆洗は、ろ材20を含む循環系内に蓄積したゴミやアルミニウム凝集物等の汚れを除去できる流速(10〜20l/min程度)と回数(一日に数回)で行なわれている。
【0021】
以下、以上のように動作する従来の循環温浴器について、図12を用いて説明する。
【0022】
図12は従来の循環温浴器の動作を示すフローチャートである。
浴槽水2の循環が開始(S1)されると、通常循環(S2)で浴槽水2が浴槽1と循環温浴器本体7間を循環してアルミニウム電解による浴槽水2の浄化が行われる。次に、循環温浴器の殺菌開始の判断(S3)を行い循環温浴器の殺菌が開始されると、制御部30により三方弁23がc→b方向に切り替えられるとともに、循環ポンプ11を停止して浴槽水2の循環を停止(S4)し、ろ過槽加熱(S5)が開始され、ろ過槽14内の殺菌処理が行われる。ここで、循環温浴器の殺菌(S3)は通常循環(S2)の間に割り込んで一日に数回切り替えられて動作する。また、電極の洗浄を行う場合にも、クエン酸等を入れて運転して洗浄するか、手洗浄をすることを割り込ませていた。
【0023】
ろ過槽加熱(S5)による殺菌処理後、制御部30により加熱殺菌循環(S6)が開始され、ろ過槽14内及び循環パイプ8,13,15a,15b,22a,22b,28内のレジオネラ属菌、大腸菌、緑膿菌等の加熱殺菌が行われる。加熱殺菌循環(S6)での加熱殺菌処理の終了後、制御部30により逆洗(S7)が開始され、ろ過槽14内を含む浴槽水2の循環系内に蓄積したゴミや汚れ及びアルミニウム凝集物等の汚れが排出口25から排出され、循環温浴器の殺菌が終了(S8)する。
【0024】
【発明が解決しようとする課題】
しかしながら、上記従来の循環温浴器では以下の課題を有していた。
【0025】
通常、電解を行うと陽極は酸性側に、陰極はアルカリ側になるが、中性の浴槽水を循環させた場合、すぐに両電極付近のpHは中性に戻る。従って、ろ過槽内で略中性の浴槽水を循環させて陽極のアルミニウム電極と陰極のSUS電極間に電流を流して浴槽水のアルミニウム電解を行った場合、アルミニウム電極の表面付近には常に略中性の浴槽水が流れるのでアルミニウム電極付近が中性となり、アルミニウム電極から溶出したアルミニウムイオンが水酸化アルミニウムになり直ちに析出する。
【0026】
このため、アルミニウム電極とSUS電極を有するろ過槽と浴槽との間で浴槽水を循環させてろ過槽中のアルミニウム電極を陽極、SUS電極を陰極として両電極間に電流を流し、浴槽水のアルミニウム電解を行い浴槽水中に水酸化アルミニウムを溶出させる動作を長期に渡って行うと、析出した水酸化アルミニウム等のスケールがアルミニウム電極の表面に付着して電解電流の低下を引き起こすとともに、浴槽水中の水酸化アルミニウムの濃度が低下して懸濁物質の凝集力が低下し、浄化性能が低下するため、浴槽水の除濁を含む安定した浄化を長期に渡って維持することが困難であるという課題を有していた。また、アルミニウム電極に付着した水酸化アルミニウム等のスケールにより浄化性能が低下するため、所定期間ごとに(1,2ヵ月に1回程度)クエン酸や酢酸、リンゴ酸等の酸でろ過槽内を洗浄してアルミニウム電極に付着したスケールを除去したり、アルミニウム電極を取り出してブラシ等で物理的に落とす必要が有り、アルミニウム電極の洗浄作業性やメンテナンス性に欠けるとともにランニングコストがかかるという課題を有していた。
【0027】
また、アルミニウム電極に付着したスケールの除去作業におけるクエン酸や酢酸、リンゴ酸等の酸(pH2〜5)によるアルミニウム電極の洗浄で循環温浴器を構成する金属部材を腐食させ、循環温浴器の耐久性に欠けるという課題を有していた。
【0028】
本発明は、上記従来の課題を解決するもので、メンテナンス性に優れ、長期に渡って安定した浄化性能を維持することができるとともに、循環温浴器の耐久性を向上できる循環温浴器の提供、及び、アルミニウム電極に水酸化アルミニウム等のスケールが付着するのを未然に防ぎ又は付着したスケールを検知してアルミニウム電極の洗浄ができる電極洗浄方法を提供することを目的とする。
【0029】
【課題を解決するための手段】
上記従来の課題を解決するために、本発明における循環温浴器は、アルミニウム電極を有したろ過槽に浴槽水を循環させてアルミニウム電解により前記浴槽水を浄化する循環温浴器であって、前記浴槽水の循環を停止してアルミニウム電解を行うことにより前記アルミニウム電極の洗浄を行う制御部を備えたものであり、長期に渡って安定した浄化性能を維持することができるとともに、該循環温浴器のメンテナンス性を向上でき、また、循環温浴器を構成する金属部材の腐食等を防止でき、循環温浴器の耐久性を向上できる。
【0030】
本発明における循環温浴器の電極洗浄方法は、アルミニウム電極を有したろ過槽に浴槽水を循環させてアルミニウム電解により前記浴槽水を浄化する循環温浴器の電極洗浄方法であって、前記ろ過槽の中の浴槽水の循環を停止させアルミニウム電解でアルミニウム電極を洗浄する電極洗浄ステップを備えたものであり、アルミニウム電極に水酸化アルミニウム等のスケールが付着するのを未然に防止できるとともに、アルミニウム電極に付着したスケールを洗浄することができる。
【0031】
【発明の実施の形態】
請求項1に記載の循環温浴器は、アルミニウム電極を有したろ過槽に浴槽水を循環させてアルミニウム電解により前記浴槽水を浄化する循環温浴器であって、前記浴槽水の循環を停止してアルミニウム電解を行うことにより前記アルミニウム電極の洗浄を行う制御部を備えており、浴槽水の循環を停止してアルミニウム電解を行うことにより、アルミニウム電極の表面への水酸化アルミニウム等のスケールの付着を防止できるとともに、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの洗浄もでき、浴槽水の浄化性能を長期に渡って維持できるという作用を有する。
【0032】
請求項2に記載の循環温浴器は、請求項1に記載の発明において、前記制御部が、前記ろ過槽を加熱するろ過槽加熱手段及び/又は、前記アルミニウム電極の電解電圧の上昇を検知する電圧検知手段を備えており、ろ過槽加熱手段によりろ過槽を加熱してアルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの溶解度を上昇でき、アルミニウム電極の表面への水酸化アルミニウム等のスケールの付着の防止やアルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの洗浄が容易にできるという作用を有する。また、電圧検知手段でアルミニウム電極の電解電圧の上昇を検知してアルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの洗浄ができるという作用を有する。
【0033】
請求項3に記載の循環温浴器は、請求項1又は2に記載の発明において、前記ろ過槽の下流側に設けられた三方弁が切り替えられて循環ポンプの上流側に配設されたプレフィルター等の上流側と前記ろ過槽の下流側が連絡されるものであり、三方弁を切り替え閉回路の循環系にして循環温浴器の加熱殺菌循環を行う際に、循環ポンプの上流側に配設されたプレフィルター等の加熱殺菌もできるという作用を有する。
【0034】
請求項4に記載の電極洗浄方法は、アルミニウム電極を有したろ過槽に浴槽水を循環させてアルミニウム電解により前記浴槽水を浄化する循環温浴器の電極洗浄方法であって、前記ろ過槽の中の浴槽水の循環を停止させアルミニウム電解でアルミニウム電極を洗浄する電極洗浄ステップを備えており、アルミニウム電極の表面付近の浴槽水のpHを2〜5まで低下させることができ、アルミニウム電極の表面への水酸化アルミニウム等のスケールの付着を防止できるとともに、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの洗浄もできるという作用を有する。
【0035】
請求項5に記載の電極洗浄方法は、請求項4に記載の発明において、前記電極洗浄ステップが、ヒータで前記ろ過槽を加熱しながら行うものであり、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの溶解度を上昇でき、アルミニウム電極への水酸化アルミニウム等のスケールの付着を防止できるとともに、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールを溶解して洗浄できるという作用を有する。
【0036】
請求項6に記載の電極洗浄方法は、請求項4に記載の発明において、前記電極洗浄ステップが、前記アルミニウム電解を停止させた後、前記ろ過槽を加熱し所定温度に加熱後アルミニウム電解を行うものであり、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの溶解度を上昇でき、アルミニウム電極への水酸化アルミニウム等のスケールの付着を防止できるとともに、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールを溶解して洗浄できるという作用を有する。
【0037】
請求項7に記載の電極洗浄方法は、請求項4乃至6の内いずれか1項に記載の発明において、前記電極洗浄ステップが、前記アルミニウム電極の電解電圧の上昇を検知した後行うものであり、アルミニウム電極への水酸化アルミニウム等のスケールの長期間に渡る付着を未然に防止できるという作用を有する。
【0038】
(実施の形態)
以下、本発明の実施の形態における循環温浴器について、図面を用いて説明する。
【0039】
図1は本発明の実施の形態における循環温浴器のシステム概略図である。尚、図7と同様のものには同一の符号を付して説明を省略する。
【0040】
図中、24′はろ過槽14の下流側の循環パイプ22bとプレフィルター6の上流側の循環パイプ28′とジェットノズル21を連結した連結点に配設された三方弁、30′はろ過槽加熱手段及び電圧検知手段を制御する制御部である。
【0041】
尚、ろ過槽14内のガラスビーズ、セラミックボール、アルミナ等の砂等からなるろ材20の粒径は0.3mm〜1mm程度のものを用いている。30μm〜40μm前後の大きさに生成されたアルミニウム電解による凝集物がろ過できる粒径のためである。
【0042】
以下、以上のように構成された循環温浴器の動作について、図面を用いて説明する。
【0043】
図2は循環温浴器の通常循環時の浴槽水の流れを示した図であり、図3は循環温浴器ろ過槽の殺菌及び電極洗浄時を示した図であり、図4は循環温浴器の加熱殺菌循環時の浴槽水の流れを示した図であり、図5は循環温浴器の逆洗時の浴槽水の流れを示した図である。
【0044】
実施の形態における循環温浴器の通常循環は、図2に示すように、従来の循環温浴器の通常循環時(図8)と同様であり、制御部30′により通常循環が開始されると、三方弁16がa→c方向、三方弁23,24′がc→a方向に切り替えられ、浴槽水2が循環ポンプ11、殺菌装置12、ろ過槽14を介してジェットノズル21から浴槽1へ排出され、浴槽1と循環温浴器本体7間で循環される。
【0045】
実施の形態における循環温浴器の殺菌及び電極洗浄では、制御部30′により三方弁23がc→b方向に切り替えられるとともに、循環ポンプ11が停止されて、図3に示すように、浴槽水2の循環が停止する。
【0046】
次に、従来のろ過槽加熱時(図9)と同様に、浴槽水2の循環停止中にろ過槽14のヒータ17(本実施の形態のろ過槽加熱手段)によりろ過槽14内の浴槽水2を温度70℃〜85℃まで加熱して、ろ過槽14内のレジオネラ属菌、緑膿菌等の殺菌が行われる。
【0047】
次いで、通常循環時にろ過槽14内において行われるアルミニウム電解と同様に、アルミニウム電極18を陽極、SUS電極19を陰極として両電極間18,19に電流を流してアルミニウム電解を行い、アルミニウム電極18の表面付近の浴槽水2のpHを2〜5まで低下させてアルミニウム電極18の洗浄を行う。
【0048】
実施の形態における加熱殺菌循環は、図4に示すように、従来の循環温浴器の加熱殺菌循環時(図10)と同様であり、制御部30′により加熱殺菌循環が開始されると、三方弁23がc→a方向、三方弁24′がc→bに切り替えられるとともに、循環ポンプ11が作動し、図4に示すように、閉回路の循環系が形成され、温度70℃〜85℃まで加熱されたろ過槽14内の浴槽水2が三方弁23,24′を介してプレフィルター6、循環ポンプ11、殺菌装置12を経てろ過槽14に再び戻り、閉回路の循環系内で循環してろ過槽14内及び循環パイプ8,13,15a,15b,22a,22b,28′内のレジオネラ属菌、大腸菌、緑膿菌等を加熱殺菌する。
【0049】
実施の形態における逆洗は、図5に示すように、従来の循環温浴器の逆洗時(図11)と同様であり、制御部30′により逆洗が開始されると、三方弁23がb→c方向、三方弁16がc→bに切り替えられ、給水口4から給水された浴槽水2が、循環パイプ8から逆洗パイプ27,三方弁23,循環パイプ22aを介してろ過槽14へ流入してろ過槽14内のろ材20に付着,蓄積したゴミや汚れ及びアルミニウム凝集物等とともに循環パイプ15b,三方弁16,逆洗パイプ26を介して排水口25から排水される。
【0050】
以下、以上のように動作する実施の形態における循環温浴器の動作について、図6を用いて説明する。
【0051】
図6は実施の形態における循環温浴器の動作を示すフローチャートである。
浴槽水2の循環が開始(S10)されると、通常循環(S11)により浴槽水2が浴槽1と循環温浴器本体7間を循環してアルミニウム電解による浴槽水2の浄化が行われる。
【0052】
次に、循環温浴器の殺菌及び電極洗浄開始の判断(S12)を行い循環温浴器ろ過槽14の殺菌及び電極洗浄が開始されると、制御部30′の電極洗浄ステップにより三方弁23がc→b方向に切り替えられるとともに、循環ポンプ11が停止してろ過槽14中の浴槽水2の循環が停止(S13)する。次に、ろ過槽14の加熱の有無を判断(S14)し、ろ過槽14の加熱をする場合は制御部の制御30′によりろ過槽14の加熱(S15)が開始される。ろ過槽14をレジオネラ属菌、緑膿菌等が殺菌できる温度70〜85℃に加熱し殺菌処理を行った後、浴槽水2の循環を停止させたままアルミニウム電解を行いアルミニウム電極18の洗浄(S16)を行う。尚、アルミニウム電極洗浄中にろ過槽14の加熱をしてもよく、また、アルミニウム電解を停止させた後にろ過槽14を加熱し、所定温度に加熱した後アルミニウム電解を行いアルミニウム電極洗浄を行なってもよい。ここで、浴槽水の循環停止(S13)、ろ過槽加熱の判断(S14)及びろ過槽加熱(S15)、アルミニウム電極洗浄(S16)からなる電極洗浄ステップは、通常循環(S11)の間に割り込んで、循環温浴器ろ過槽14及び浴槽水2中の菌の増殖を抑えることのできる殺菌回数(例えば、4時間毎に1回,1日に6回)、又は制御部30′の電圧制御手段でアルミニウム電極18の電解電圧の上昇を検知した後に行われる。
【0053】
電極洗浄ステップのアルミニウム電極洗浄(S16)による電極洗浄後、制御部30′により加熱殺菌循環(S17)が開始され、ろ過槽14内及び循環パイプ8,13,15a,15b,22a,22b,28′内のレジオネラ属菌、大腸菌、緑膿菌等の加熱殺菌が行われる。加熱殺菌循環(S17)での加熱殺菌処理の終了後、制御部30′により逆洗(S18)が開始され、ろ過槽14内を含む浴槽水2の循環系内に蓄積したゴミや汚れ及びアルミニウム凝集物等の汚れが排出口25から排出され、循環温浴器の殺菌及び電極洗浄が終了(S19)する。
【0054】
以上のように本実施の形態によれば、通常循環の間に割り込んで行う循環温浴器ろ過槽の殺菌及び電極洗浄時における電極洗浄ステップで、浴槽水の循環を停止して循環停止中にアルミニウム電解を行うことにより、循環すると中性に近づくアルミニウム電極の表面付近の浴槽水のpHを2〜5まで低下することができ、アルミニウム電極の表面のアルミニウムの状態を3価アルミニウムイオンにすることができ、アルミニウム電極の表面に水酸化アルミニウムが付着するのを防止できるという作用を有する。また、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールを溶解して洗浄できるという作用を有する。
【0055】
また、アルミニウム電極洗浄中に、ろ過槽内の浴槽水を加熱することにより、更に、アルミニウム電極に付着した水酸化アルミニウム等のスケールの溶解度を上昇でき、アルミニウム電極の表面の水酸化アルミニウム等のスケールの付着を防止または付着した水酸化アルミニウム等のスケールを容易に洗浄できるという作用を有する。
【0056】
また、三方弁がろ過槽の下流側とプレフィルターの上流側とジェットノズルを連結した連結点に配設されているため、加熱殺菌循環時にプレフィルターの殺菌処理ができるという作用を有する。
【0057】
尚、本実施の形態におけるろ過槽と同様の構成と洗浄方法を有する排水及び厨芥のss成分を除去する装置の場合にも本発明の作用、効果が得られる。
【0058】
【発明の効果】
以上のように本発明によれば、以下の優れた効果を得ることができる。
【0059】
請求項1に記載の発明によれば、浴槽水の循環を停止してアルミニウム電解を行うことにより、アルミニウム電極の表面への水酸化アルミニウム等のスケールの付着を防止できるとともに、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの洗浄もでき、従来のように定期的にクエン酸や酢酸、リンゴ酸等の酸(pH2〜5)でアルミニウム電極を洗浄したり、アルミニウム電極を取り出してブラシ等で物理的にスケール等を取り除く作業を要さず、ランニングコストを低下でき、メンテナンス性に優れるとともに、循環温浴器の金属部材の腐食等を防ぎ、循環温浴器の耐久性を向上できる。
【0060】
請求項2に記載の発明によれば、請求項1の効果に加えて、ろ過槽加熱手段によりろ過槽を加熱してアルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの溶解度を上昇でき、アルミニウム電極の表面への水酸化アルミニウム等のスケールの付着の防止やアルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの洗浄が容易にでき、循環温浴器の浄化性能を長期に渡って安定して維持できるとともに、効率の良いアルミニウム電解を行なうことができ、浴槽水の浄化性能(凝集効果)の向上が図れる。
【0061】
また、電圧検知手段でアルミニウム電極の電解電圧の上昇を検知してアルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの洗浄ができ、アルミニウム電極へのスケールの付着状況に応じて自動的にアルミニウム電極の洗浄ができメンテナンス性に優れる。
【0062】
請求項3に記載発明によれば、請求項1又は2の効果に加えて、三方弁を切り替え閉回路の循環系にして循環温浴器の加熱殺菌循環を行う際に、循環ポンプの上流側に配設されたプレフィルター等の加熱殺菌もでき、循環温浴器の衛生に優れる。
【0063】
請求項4に記載の発明によれば、アルミニウム電極の表面付近の浴槽水のpHを2〜5まで低下させることができ、アルミニウム電極の表面への水酸化アルミニウム等のスケールの付着を防止できるとともに、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの洗浄もでき、アルミニウム電極の洗浄作業性に優れるとともに、アルミニウム電極の性能を維持できる。
【0064】
請求項5に記載の発明によれば、請求項4の効果に加えて、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの溶解度を上昇でき、アルミニウム電極への水酸化アルミニウム等のスケールの付着を防止できるとともに、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールを溶解して洗浄でき、アルミニウム電極及び循環温浴器の浄化を容易に短時間で行うことができメンテナンス性に優れる。
【0065】
請求項6に記載の発明によれば、請求項4の効果に加えて、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールの溶解度を上昇でき、アルミニウム電極への水酸化アルミニウム等のスケールの付着を防止できるとともに、アルミニウム電極の表面に付着した水酸化アルミニウム等のスケールを溶解して洗浄できる。
【0066】
請求項7に記載の発明によれば、請求項4乃至6の効果に加えて、アルミニウム電極への水酸化アルミニウム等のスケールの付着を未然に防止でき、長期に渡って電解電流の低下を防いで無駄な電解電圧をかける必要がなくなり、長期間安定した浄化性能を得ることができるとともに、効率の良いアルミニウム電解を行なうことができ、浄化性能(凝集効果)の向上も図れる。
【図面の簡単な説明】
【図1】本発明の実施の形態における循環温浴器のシステム概略図
【図2】循環温浴器の通常循環時の浴槽水の流れを示した図
【図3】循環温浴器ろ過槽の殺菌及び電極洗浄時を示した図
【図4】循環温浴器の加熱殺菌循環時の浴槽水の流れを示した図
【図5】循環温浴器の逆洗時の浴槽水の流れを示した図
【図6】実施の形態における循環温浴器の動作を示すフローチャート
【図7】従来の循環温浴器のシステム概略図
【図8】循環温浴器の通常循環時の浴槽水の流れを示した図
【図9】循環温浴器ろ過槽の殺菌時を示した図
【図10】循環温浴器の加熱殺菌循環時の浴槽水の流れを示した図
【図11】循環温浴器の逆洗時の浴槽水の流れを示した図
【図12】従来の循環温浴器の動作を示すフローチャート
【符号の説明】
1 浴槽
2 浴槽水
3 ノズルユニット
4 給水口
5 逆止弁
6 プレフィルター(ヘアーキャッチャー)
7 循環温浴器本体
8 循環パイプ
9 流量センサー
10,17a 温度センサー
11 循環ポンプ
12 殺菌装置
13 循環パイプ
15a,15b 循環パイプ
14 ろ過槽
16,23,24,24′ 三方弁
17 ヒータ
18 アルミニウム電極
19 SUS電極
20 ろ材
21 ジェットノズル
22a,22b,22c 循環パイプ
25 逆洗排水口
26,27 逆洗パイプ
28,28′ 循環パイプ
29 電源部
30,30′ 制御部
31 表示及び操作部
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a circulating bath and an electrode cleaning method that have functions of aggregating treatment (purification) by aluminum electrolysis and heat insulation, and circulating and reusing bath water of a bath.
[0002]
[Prior art]
In recent years, bath water once used has been circulated through pre-filters (hair catchers), filtration tanks, activation tanks, heaters, etc. using a circulation pump to remove, activate, and heat the bathtub water. Circulating baths for heat insulation have come to be used in general household baths.
[0003]
At present, most circulating hot water baths in the market purify and deodorize bathtub water using biological treatment, but those that perform agglomeration treatment by aluminum electrolysis have also attracted attention. In addition to removing dirt from bath water, it is necessary to prevent the generation of malodors, E. coli, Legionella spp., Pseudomonas aeruginosa, etc. Those that are provided with ozone treatment, those that are sterilized with silver antibacterial agents, and those that are equipped with an electrolyzer that electrolyzes the bath water to return acid water to the bath water, etc. have been developed Yes.
[0004]
Hereinafter, a conventional circulating warm bath using aluminum electrolysis will be described with reference to the drawings.
[0005]
FIG. 7 is a schematic system diagram of a conventional circulating bath.
In the figure, 1 is a bathtub, 2 is bathtub water, 3 is a nozzle unit disposed in the bathtub 1, 4 is a water supply port through which the bathtub water 2 is supplied into the nozzle unit 3, and 5 is supplied from the water supply port 4. A check valve for preventing the reverse flow of the bathtub water 2, 6 is a pre-filter (hair catcher) made of a mesh mesh made of a resin such as sponge or polypropylene, a spool filter, and 7 is connected to the nozzle unit 3 via a circulation pipe 8. A conventional circulating hot water bath body connected, 9 is a flow sensor for detecting the flow rate of the bath water 2 from the nozzle unit 3 provided in the circulating pipe 8, 10 is a temperature sensor, and 11 is a circulating pump of the circulating hot water bath body 7. , 12 is a sterilizer for sterilizing and deodorizing the bathtub water 2 sent from the circulation pump 11 using ultraviolet rays or ozone, 13 is a circulation pipe connecting the circulation pump 11 and the sterilizer 12, and 14 is An excess tank, 15a and 15b are circulation pipes connecting the sterilizer 12 and the filtration tank 14, 16 is a three-way valve disposed at a connection point of the circulation pipes 15a and 15b, and 17 is for heat sterilization and heat insulation of the filtration tank 14. The heater 17a is a temperature sensor of the filtration tank 14, 18 is an aluminum electrode disposed in the filtration tank 14, 19 is a SUS electrode disposed in the filtration tank 14, and 20 is disposed in the filtration tank 14. Filter medium made of sand such as glass beads, ceramic balls, alumina, etc., 21 is a jet nozzle that returns the bathtub water 2 circulated in the circulating bath body 7 to the bathtub 1, and 22a, 22b, 22c are the circulating bath body 7 and jet. A circulation pipe to which the nozzle 21 is connected, 23 is a three-way valve disposed at the connection point of the circulation pipes 22a and 22b, 24 is a three-way valve disposed at the connection point of the circulation pipes 22b and 22c, and 25 is Backwash drain for draining the wash water that washed the circulating bath body 7, 26 is a backwash pipe connecting the three-way valve 16 and the backwash drain 25, and 27 is a backwash connecting the three-way valve 23 and the circulation pipe 13. Pipe, 28 is a circulation pipe connecting the three-way valve 24 and the circulation pipe 8, 29 is a power supply unit of the circulation warm bath main body 7, 30 is a control unit of the circulation warm bath main body 7, and 31 is a display and operation of the circulation warm bath main body 7. Part.
[0006]
Hereinafter, the operation of the conventional circulating warm bath configured as described above will be described with reference to the drawings.
[0007]
FIG. 8 is a diagram showing the flow of bath water during normal circulation of the circulating hot water bath, FIG. 9 is a diagram showing the time of sterilization of the circulating hot water bath filter tank, and FIG. 10 is the heat sterilization circulation of the circulating hot water bath. It is the figure which showed the flow of the bathtub water at the time, and FIG. 11 is the figure which showed the flow of the bathtub water at the time of the backwashing of a circulation warm bath.
[0008]
First, the normal circulation of the circulating bath will be described with reference to FIG.
When the normal circulation operation is started by the control unit 30, the three-way valve 16 is switched in the a → c direction, and the three-way valves 23 and 24 are switched in the c → a direction. Next, the circulation pump 11 is driven, and the bathtub water 2 in the bathtub 1 is sucked up from the water supply port 4 of the nozzle unit 3, passes through the prefilter 6, and the hair such as hair contained in the bathtub water 2 is large by the prefilter 6. Dust is collected and further flows into the circulation pump 11 through the flow pipe 9 and the temperature sensor 10 via the circulation pipe 8.
[0009]
Here, in order to prevent a decrease in the circulation flow rate, the prefilter 6 (especially when it is made of sponge or the like) is periodically taken out once every 1 or 2 weeks to remove large dust such as attached hair. . Further, in the case of the prefilter 6 composed of a pincushion filter, when the circulating flow rate of the bathtub water 2 falls below a certain flow rate, it is detected by the control unit 30 and the time for cleaning or replacing the prefilter 6 by the display and operation unit 31 is detected. it's shown.
[0010]
Next, the bathtub water 2 sent out from the circulation pump 11 is sterilized and deodorized by the sterilizer 12 using ultraviolet light, ozone, or the like, and flows into the filtration tank 14 through the three-way valve 16.
[0011]
In the filtration tank 14, the aluminum electrode 18 is used as an anode and the SUS electrode 19 is used as a cathode to conduct an electric current between both electrodes to perform aluminum electrolysis of the bath water 2, and aluminum hydroxide is eluted into the bath water 2. Aluminum is used to agglomerate small dust and dirt (organic substances such as inorganic substances, proteins and lipids) which are suspended in the bathtub water 2. Next, aggregates such as small dust and dirt (organic substances such as inorganic substances, proteins and lipids) that could not be removed by the prefilter 6 by the filter medium 20 made of glass beads, ceramic balls, sand such as alumina, etc. in the filtration tank 14. Filtered (generally referred to as purification). The temperature of the bathtub water 2 is controlled by a heater 17 and a temperature sensor 17a for heat sterilization and heat retention of the filtration tank 14.
[0012]
The bathtub water 2 purified in the filtration tank 14 is returned from the jet nozzle 21 to the bathtub 1 through the three-way valves 23 and 24.
[0013]
Next, the sterilization of the circulating warm bath filter tank 14 will be described with reference to FIG.
When the sterilization of the circulating warm bath filter tank 14 is started by the control unit 30, the three-way valve 23 is switched in the c → b direction, the circulation pump 11 is stopped, and the circulation of the bath water 2 is stopped.
[0014]
Next, the bath water 2 in the filtration tank 14 is heated to a temperature of 70 ° C. to 85 ° C. by the heater 17 of the filtration tank 14 to sterilize Legionella and Pseudomonas aeruginosa in the filtration tank 14. The electrode is washed by adding citric acid, acetic acid, malic acid or the like to the bath water 2 as needed to circulate and take the scale, or by taking out the electrode and washing it manually.
[0015]
Next, the heat sterilization circulation of the circulating bath will be described with reference to FIG.
When the heat sterilization circulation operation is started by the control unit 30, the three-way valve 23 is switched in the c → a direction and the three-way valve 24 is switched in the c → b direction, and the circulation pump 11 is operated to close as shown in FIG. A circuit circulation system is formed.
[0016]
The bath water 2 in the filtration tank 14 heated to a temperature of 70 ° C. to 85 ° C. returns again to the filtration tank 14 through the circulation pump 11 and the sterilizer 12 via the three-way valves 23 and 24, and in the closed circuit circulation system. It circulates and heat-sterilizes Legionella, Escherichia coli, Pseudomonas aeruginosa and the like in the filtration tank 14 and the circulation pipes 8, 13, 15a, 15b, 22a, 22b, 28.
[0017]
Next, the backwashing of the circulating bath will be described with reference to FIG.
When the backwashing operation is started by the control unit 30, the three-way valve 23 is switched in the b → c direction, and the three-way valve 16 is switched from c → b.
[0018]
The bath water 2 supplied from the water supply port 4 by the circulation pump 11 is supplied from the circulation pipe 8 provided with the flow sensor 9 and the temperature sensor 10 to the filtration tank 14 through the backwash pipe 27, the three-way valve 23, and the circulation pipe 22a. Flow into.
[0019]
The bathtub water 2 flowing into the filtration tank 14 from the circulation pipe 22a adheres to the filter medium 20 in the filtration tank 14 and accumulates dust, dirt, aluminum agglomerates, etc., along the circulation pipe 15b, the three-way valve 16, and the backwash pipe 26. The water is drained from the drainage port 25.
[0020]
The backwashing is performed at a flow rate (about 10 to 20 l / min) and the number of times (several times a day) that can remove dirt accumulated in the circulation system including the filter medium 20 and aluminum aggregates. .
[0021]
Hereinafter, a conventional circulating warm bath that operates as described above will be described with reference to FIG.
[0022]
FIG. 12 is a flowchart showing the operation of the conventional circulating bath.
When the circulation of the bathtub water 2 is started (S1), the bathtub water 2 is circulated between the bathtub 1 and the circulation warm bath body 7 in the normal circulation (S2), and the purification of the bathtub water 2 by aluminum electrolysis is performed. Next, when the sterilization of the circulating water bath is started (S3) and the sterilization of the circulating water bath is started, the three-way valve 23 is switched in the c → b direction by the control unit 30 and the circulation pump 11 is stopped. Then, the circulation of the bathtub water 2 is stopped (S4), the filtration tank heating (S5) is started, and the sterilization process in the filtration tank 14 is performed. Here, the sterilization (S3) of the circulating bath is operated by switching several times a day while interrupting the normal circulation (S2). In addition, when cleaning the electrode, it has been interrupted to operate by washing with citric acid or the like, or to perform manual cleaning.
[0023]
After the sterilization treatment by the filtration tank heating (S5), the control unit 30 starts the heat sterilization circulation (S6), and Legionella in the filtration tank 14 and the circulation pipes 8, 13, 15a, 15b, 22a, 22b, 28. Then, heat sterilization of Escherichia coli, Pseudomonas aeruginosa, etc. is performed. After completion of the heat sterilization process in the heat sterilization circulation (S6), backwashing (S7) is started by the control unit 30, and dust and dirt accumulated in the circulation system of the bath water 2 including the inside of the filtration tank 14 and aluminum aggregation Dirt such as objects is discharged from the discharge port 25, and the sterilization of the circulating bath is completed (S8).
[0024]
[Problems to be solved by the invention]
However, the conventional circulating bath has the following problems.
[0025]
Usually, when electrolysis is performed, the anode is on the acidic side and the cathode is on the alkaline side, but when neutral bath water is circulated, the pH in the vicinity of both electrodes immediately returns to neutral. Accordingly, when aluminum electrolysis of bathtub water is performed by circulating substantially neutral bathtub water in the filtration tank and passing a current between the aluminum electrode of the anode and the SUS electrode of the cathode, the surface of the aluminum electrode is always substantially omitted. Since neutral bath water flows, the vicinity of the aluminum electrode becomes neutral, and aluminum ions eluted from the aluminum electrode become aluminum hydroxide and immediately precipitate.
[0026]
For this reason, the bathtub water is circulated between a filtration tank having an aluminum electrode and a SUS electrode and the bathtub, and an aluminum electrode in the filtration tank is used as an anode and a current is passed between both electrodes using the SUS electrode as a cathode. If electrolysis is performed and aluminum hydroxide is eluted in the bath water over a long period of time, the deposited aluminum hydroxide scale adheres to the surface of the aluminum electrode, causing a decrease in the electrolysis current and the water in the bath water. The problem is that it is difficult to maintain stable purification including turbidity of bath water over a long period of time because the concentration of aluminum oxide is reduced, the cohesive power of suspended substances is reduced, and purification performance is reduced. Had. In addition, since the purification performance is reduced by the scale of aluminum hydroxide or the like attached to the aluminum electrode, the inside of the filter tank is filled with acid such as citric acid, acetic acid or malic acid every predetermined period (about once every 1 or 2 months). It is necessary to remove the scale attached to the aluminum electrode by cleaning, or to take out the aluminum electrode and physically remove it with a brush, etc. Was.
[0027]
In addition, the metal member constituting the circulating bath is corroded by washing the aluminum electrode with an acid (pH 2 to 5) such as citric acid, acetic acid, malic acid, etc. in the removal work of the scale attached to the aluminum electrode, and the durability of the circulating bath It had the problem of lacking in nature.
[0028]
The present invention solves the above-mentioned conventional problems, and provides a circulating hot water bath that is excellent in maintainability, can maintain stable purification performance over a long period of time, and can improve the durability of the circulating hot water bath, Another object of the present invention is to provide an electrode cleaning method capable of preventing the scale of aluminum hydroxide or the like from adhering to the aluminum electrode or cleaning the aluminum electrode by detecting the adhered scale.
[0029]
[Means for Solving the Problems]
In order to solve the above-described conventional problems, the circulating hot water bath in the present invention is a circulating hot water bath that circulates bathtub water in a filtration tank having an aluminum electrode and purifies the bathtub water by aluminum electrolysis. A control unit for cleaning the aluminum electrode by stopping the water circulation and performing aluminum electrolysis can maintain a stable purification performance over a long period of time. Maintenance can be improved, corrosion of the metal member constituting the circulating bath can be prevented, and durability of the circulating bath can be improved.
[0030]
An electrode cleaning method for a circulating warm bath according to the present invention is an electrode cleaning method for a circulating warm bath that circulates bathtub water in a filtration tank having an aluminum electrode and purifies the bathtub water by aluminum electrolysis. It is equipped with an electrode cleaning step that stops the circulation of the bath water in the interior and cleans the aluminum electrode by aluminum electrolysis, and prevents the aluminum electrode and the like from adhering to the aluminum electrode. The attached scale can be washed.
[0031]
DETAILED DESCRIPTION OF THE INVENTION
The circulating warm bath according to claim 1 is a circulating warm bath that circulates bathtub water in a filtration tank having an aluminum electrode and purifies the bathtub water by aluminum electrolysis, and stops circulation of the bathtub water. A control unit for cleaning the aluminum electrode by performing aluminum electrolysis is provided, and the scale of aluminum hydroxide or the like adheres to the surface of the aluminum electrode by stopping the circulation of bath water and performing aluminum electrolysis. In addition to being able to prevent, scales such as aluminum hydroxide adhering to the surface of the aluminum electrode can be washed, and the purification performance of the bath water can be maintained over a long period of time.
[0032]
According to a second aspect of the present invention, in the circulating hot water bath according to the first aspect, the control unit detects a rise in the electrolytic voltage of the filter tank heating means and / or the aluminum electrode for heating the filter tank. Equipped with voltage detection means, heating the filtration tank by the filtration tank heating means can increase the solubility of scales such as aluminum hydroxide adhering to the surface of the aluminum electrode, the scale of aluminum hydroxide etc. on the surface of the aluminum electrode It is possible to prevent the adhesion of aluminum and to easily clean scales such as aluminum hydroxide adhering to the surface of the aluminum electrode. In addition, the voltage detecting means detects an increase in the electrolytic voltage of the aluminum electrode, and has an effect that the scale such as aluminum hydroxide adhered to the surface of the aluminum electrode can be cleaned.
[0033]
According to a third aspect of the present invention, there is provided a pre-filter in which the three-way valve provided on the downstream side of the filtration tank is switched and the upstream side of the circulation pump is switched. The upstream side of the filtration tank and the downstream side of the filtration tank are connected to each other, and are arranged upstream of the circulation pump when the three-way valve is switched and the circulation system of the closed circuit is used for heat sterilization circulation. It also has the effect of being able to sterilize by heating such as a prefilter.
[0034]
The electrode cleaning method according to claim 4 is an electrode cleaning method for a circulating warm bath that circulates bathtub water in a filtration tank having an aluminum electrode and purifies the bathtub water by aluminum electrolysis. An electrode cleaning step for stopping the circulation of the bathtub water and cleaning the aluminum electrode by aluminum electrolysis, and the pH of the bath water in the vicinity of the surface of the aluminum electrode can be lowered to 2-5, to the surface of the aluminum electrode It is possible to prevent the scale such as aluminum hydroxide from adhering to the surface and to clean the scale such as aluminum hydroxide adhered to the surface of the aluminum electrode.
[0035]
According to a fifth aspect of the present invention, there is provided the electrode cleaning method according to the fourth aspect, wherein the electrode cleaning step is performed while heating the filtration tank with a heater, and the aluminum hydroxide adhered to the surface of the aluminum electrode It is possible to increase the solubility of the scale such as aluminum hydroxide, to prevent the scale such as aluminum hydroxide from adhering to the aluminum electrode, and to dissolve and wash the scale such as aluminum hydroxide adhered to the surface of the aluminum electrode.
[0036]
The electrode cleaning method according to claim 6 is the invention according to claim 4, wherein after the electrode cleaning step stops the aluminum electrolysis, the filtration tank is heated to a predetermined temperature and then subjected to aluminum electrolysis. It is possible to increase the solubility of scales such as aluminum hydroxide adhering to the surface of the aluminum electrode, while preventing the adhesion of scales such as aluminum hydroxide to the aluminum electrode, and aluminum hydroxide adhering to the surface of the aluminum electrode It has an effect that it can be dissolved and washed.
[0037]
The electrode cleaning method according to claim 7 is performed in the invention according to any one of claims 4 to 6 after the electrode cleaning step detects an increase in electrolytic voltage of the aluminum electrode. In addition, it has an effect that it is possible to prevent adhesion of a scale such as aluminum hydroxide to the aluminum electrode over a long period of time.
[0038]
(Embodiment)
Hereinafter, the circulating bath in the embodiment of the present invention will be described with reference to the drawings.
[0039]
FIG. 1 is a system schematic diagram of a circulating warm bath in the embodiment of the present invention. In addition, the same code | symbol is attached | subjected to the thing similar to FIG. 7, and description is abbreviate | omitted.
[0040]
In the figure, 24 'is a three-way valve disposed at a connection point connecting the circulation pipe 22b on the downstream side of the filtration tank 14, the circulation pipe 28' on the upstream side of the prefilter 6 and the jet nozzle 21, and 30 'is the filtration tank. It is a control part which controls a heating means and a voltage detection means.
[0041]
The filter medium 20 made of glass beads, ceramic balls, sand such as alumina in the filtration tank 14 has a particle size of about 0.3 mm to 1 mm. This is because the agglomerates produced by aluminum electrolysis having a size of about 30 μm to 40 μm can be filtered.
[0042]
Hereinafter, the operation of the circulating warm bath configured as described above will be described with reference to the drawings.
[0043]
FIG. 2 is a diagram showing the flow of bath water during normal circulation of the circulating hot water bath, FIG. 3 is a diagram showing sterilization of the circulating hot water bath filter tank and electrode cleaning, and FIG. 4 is a diagram of the circulating hot water bath. It is the figure which showed the flow of the bathtub water at the time of heat sterilization circulation, and FIG. 5 is the figure which showed the flow of the bathtub water at the time of backwashing of a circulating warm bath.
[0044]
As shown in FIG. 2, the normal circulation of the circulating warm bath in the embodiment is the same as that of the conventional circulating warm bath (FIG. 8), and when the normal circulation is started by the control unit 30 ′, The three-way valve 16 is switched to the a → c direction and the three-way valves 23 and 24 ′ are switched to the c → a direction, and the bathtub water 2 is discharged from the jet nozzle 21 to the bathtub 1 through the circulation pump 11, the sterilizer 12, and the filtration tank 14. And is circulated between the bathtub 1 and the circulating bath body 7.
[0045]
In the sterilization of the circulating hot water bath and the electrode cleaning in the embodiment, the three-way valve 23 is switched in the c → b direction by the control unit 30 ′, and the circulation pump 11 is stopped. As shown in FIG. Circulation stops.
[0046]
Next, the bath water in the filtration tank 14 is heated by the heater 17 of the filtration tank 14 (the filtration tank heating means of the present embodiment) while the circulation of the bathtub water 2 is stopped, as in the conventional heating of the filtration tank (FIG. 9). 2 is heated to a temperature of 70 ° C. to 85 ° C. to sterilize Legionella spp., Pseudomonas aeruginosa and the like in the filtration tank 14.
[0047]
Next, similarly to the aluminum electrolysis performed in the filtration tank 14 during normal circulation, the aluminum electrode 18 is used as an anode, the SUS electrode 19 is used as a cathode, and current is passed between the two electrodes 18, 19 to perform aluminum electrolysis. The aluminum electrode 18 is cleaned by lowering the pH of the bathtub water 2 near the surface to 2-5.
[0048]
As shown in FIG. 4, the heat sterilization circulation in the embodiment is the same as that during the heat sterilization circulation of the conventional circulation bath (FIG. 10). The valve 23 is switched from c to a and the three-way valve 24 'is switched from c to b, and the circulation pump 11 is operated to form a closed circuit circulation system as shown in FIG. The bath water 2 in the filtration tank 14 heated up to 3 is returned to the filtration tank 14 through the pre-filter 6, the circulation pump 11 and the sterilizer 12 through the three-way valves 23 and 24 ', and circulated in the closed circuit circulation system. Then, Legionella spp., Escherichia coli, Pseudomonas aeruginosa and the like in the filtration tank 14 and the circulation pipes 8, 13, 15a, 15b, 22a, 22b, 28 'are sterilized by heating.
[0049]
As shown in FIG. 5, the backwashing in the embodiment is the same as the backwashing of the conventional circulating bath (FIG. 11). When the backwashing is started by the control unit 30 ', the three-way valve 23 is turned on. In the b → c direction, the three-way valve 16 is switched from c → b, and the bathtub water 2 supplied from the water supply port 4 is filtered from the circulation pipe 8 through the backwash pipe 27, the three-way valve 23, and the circulation pipe 22a. It is drained from the drain port 25 through the circulation pipe 15b, the three-way valve 16, and the backwash pipe 26 together with dust, dirt, aluminum aggregates, and the like that have flowed into the filter tank 14 and adhered to the filter medium 20 in the filter tank 14.
[0050]
Hereinafter, the operation of the circulating bath in the embodiment operating as described above will be described with reference to FIG.
[0051]
FIG. 6 is a flowchart showing the operation of the circulating warm bath in the embodiment.
When the circulation of the bathtub water 2 is started (S10), the bathtub water 2 is circulated between the bathtub 1 and the circulation warm bath body 7 by the normal circulation (S11), and the purification of the bathtub water 2 by aluminum electrolysis is performed.
[0052]
Next, when the sterilization and electrode cleaning of the circulating hot water bath filtration tank 14 are started by determining whether the circulating hot water bath is sterilized and electrode cleaning is started (S12), the three-way valve 23 is turned on by the electrode cleaning step of the control unit 30 '. While being switched to the b direction, the circulation pump 11 stops and the circulation of the bath water 2 in the filtration tank 14 stops (S13). Next, it is determined whether or not the filtration tank 14 is heated (S14). When the filtration tank 14 is heated, the control section 30 'starts heating the filtration tank 14 (S15). The filtration tank 14 is heated to a temperature of 70 to 85 ° C. at which Legionella spp., Pseudomonas aeruginosa, etc. can be sterilized and then sterilized, and then the aluminum electrode 18 is washed while the circulation of the bath water 2 is stopped ( S16) is performed. The filtration tank 14 may be heated during the aluminum electrode cleaning, or after the aluminum electrolysis is stopped, the filtration tank 14 is heated, heated to a predetermined temperature, and then subjected to aluminum electrolysis to clean the aluminum electrode. Also good. Here, the electrode cleaning step comprising the bath water circulation stop (S13), the filtration tank heating determination (S14), the filtration tank heating (S15), and the aluminum electrode cleaning (S16) is interrupted during the normal circulation (S11). Thus, the number of times of sterilization (for example, once every 4 hours, 6 times a day) or the voltage control means of the control unit 30 'can suppress the growth of bacteria in the circulating bath filter 14 and the bath water 2. This is performed after detecting the increase in the electrolysis voltage of the aluminum electrode 18.
[0053]
After electrode cleaning by the aluminum electrode cleaning (S16) of the electrode cleaning step, the heat sterilization circulation (S17) is started by the control unit 30 ', and the inside of the filtration tank 14 and the circulation pipes 8, 13, 15a, 15b, 22a, 22b, 28 are started. The heat sterilization of Legionella spp., Escherichia coli, Pseudomonas aeruginosa, etc. in the ′ is performed. After completion of the heat sterilization process in the heat sterilization circulation (S17), backwashing (S18) is started by the control unit 30 ', and dust and dirt accumulated in the circulation system of the bathtub water 2 including the inside of the filtration tank 14 and aluminum Dirt such as agglomerates is discharged from the discharge port 25, and the sterilization and electrode cleaning of the circulating bath are completed (S19).
[0054]
As described above, according to the present embodiment, in the electrode cleaning step during the sterilization and electrode cleaning of the circulating warm bath filter tank that is interrupted during the normal circulation, the bath water circulation is stopped and the aluminum is stopped during the circulation stop. By performing electrolysis, the pH of the bath water near the surface of the aluminum electrode that approaches neutrality when circulating can be lowered to 2-5, and the state of aluminum on the surface of the aluminum electrode can be changed to trivalent aluminum ions. And has the effect of preventing aluminum hydroxide from adhering to the surface of the aluminum electrode. Moreover, it has the effect | action which melt | dissolves and wash | cleans scales, such as aluminum hydroxide adhering to the surface of the aluminum electrode.
[0055]
In addition, by heating the bath water in the filtration tank during the cleaning of the aluminum electrode, the solubility of the scale such as aluminum hydroxide attached to the aluminum electrode can be further increased, and the scale such as aluminum hydroxide on the surface of the aluminum electrode can be increased. It has an effect that scales such as aluminum hydroxide can be easily washed.
[0056]
Further, since the three-way valve is disposed at a connection point connecting the downstream side of the filtration tank, the upstream side of the prefilter, and the jet nozzle, it has an effect that the prefilter can be sterilized during the heat sterilization circulation.
[0057]
In addition, the effect | action and effect of this invention are acquired also in the case of the apparatus which removes the ss component of the waste_water | drain and the soot which has the structure and washing | cleaning method similar to the filtration tank in this Embodiment.
[0058]
【The invention's effect】
As described above, according to the present invention, the following excellent effects can be obtained.
[0059]
According to the first aspect of the invention, by stopping the circulation of the bath water and performing aluminum electrolysis, it is possible to prevent adhesion of scale such as aluminum hydroxide to the surface of the aluminum electrode, and to the surface of the aluminum electrode. The scale of adhered aluminum hydroxide can be cleaned, and the aluminum electrode is periodically cleaned with acids (pH 2 to 5) such as citric acid, acetic acid and malic acid as in the past, or the aluminum electrode is taken out and brushed. Therefore, it is not necessary to physically remove the scale and the like, the running cost can be reduced, the maintainability is excellent, the corrosion of the metal member of the circulating bath is prevented, and the durability of the circulating bath is improved.
[0060]
According to invention of Claim 2, in addition to the effect of Claim 1, the solubility of scales, such as aluminum hydroxide which heated the filtration tank by the filtration tank heating means and adhered to the surface of an aluminum electrode, can be raised, Prevents the adhesion of aluminum hydroxide and other scales to the surface of the aluminum electrode and facilitates cleaning of the aluminum hydroxide and other scales attached to the surface of the aluminum electrode, and stabilizes the purification performance of the circulating bath for a long period of time. In addition, it is possible to perform efficient aluminum electrolysis and improve the purification performance (coagulation effect) of the bath water.
[0061]
In addition, the voltage detection means detects the increase in the electrolysis voltage of the aluminum electrode and can clean the scale such as aluminum hydroxide adhering to the surface of the aluminum electrode. The electrode can be cleaned and is easy to maintain.
[0062]
According to the third aspect of the present invention, in addition to the effect of the first or second aspect, when performing the heat sterilization circulation of the circulating warm bath using the three-way valve as a closed circuit circulation system, the upstream side of the circulation pump is provided. Heat disinfection of the prefilter and the like can be performed, and the hygiene of the circulating bath is excellent.
[0063]
According to the invention of claim 4, the pH of the bath water near the surface of the aluminum electrode can be lowered to 2 to 5, and the adhesion of scale such as aluminum hydroxide to the surface of the aluminum electrode can be prevented. In addition, the scale of aluminum hydroxide or the like attached to the surface of the aluminum electrode can be cleaned, and the cleaning performance of the aluminum electrode is excellent, and the performance of the aluminum electrode can be maintained.
[0064]
According to the fifth aspect of the invention, in addition to the effect of the fourth aspect, the solubility of the scale such as aluminum hydroxide attached to the surface of the aluminum electrode can be increased, and the scale of the aluminum hydroxide or the like on the aluminum electrode can be increased. In addition to preventing adhesion, scales such as aluminum hydroxide adhered to the surface of the aluminum electrode can be dissolved and washed, and the aluminum electrode and the circulating warm bath can be easily purified in a short period of time, resulting in excellent maintainability.
[0065]
According to the sixth aspect of the invention, in addition to the effect of the fourth aspect, the solubility of the scale such as aluminum hydroxide adhered to the surface of the aluminum electrode can be increased, and the scale of the aluminum hydroxide or the like on the aluminum electrode can be increased. Adhesion can be prevented and scales such as aluminum hydroxide adhering to the surface of the aluminum electrode can be dissolved and washed.
[0066]
According to the seventh aspect of the invention, in addition to the effects of the fourth to sixth aspects, it is possible to prevent adhesion of scale such as aluminum hydroxide to the aluminum electrode, and to prevent a decrease in electrolytic current over a long period of time. Therefore, it is not necessary to apply a useless electrolysis voltage, and a stable purification performance can be obtained for a long period of time, an efficient aluminum electrolysis can be performed, and the purification performance (coagulation effect) can be improved.
[Brief description of the drawings]
FIG. 1 is a system schematic diagram of a circulating warm bath in an embodiment of the present invention.
FIG. 2 is a diagram showing the flow of bathtub water during normal circulation of a circulating bath
FIG. 3 is a diagram showing sterilization and electrode cleaning of a circulating bath filter tank
FIG. 4 is a diagram showing the flow of bathtub water during the heat sterilization circulation of the circulating bath
FIG. 5 shows the flow of bathtub water during backwashing of a circulating bath
FIG. 6 is a flowchart showing the operation of the circulating warm bath in the embodiment.
FIG. 7 is a schematic diagram of a conventional circulating bath system.
FIG. 8 is a diagram showing the flow of bathtub water during normal circulation of a circulating water bath
FIG. 9 is a diagram showing the sterilization of the circulating bath filter tank
FIG. 10 is a diagram showing the flow of bathtub water during the heat sterilization circulation of the circulating bath
FIG. 11 shows the flow of bathtub water during backwashing of a circulating bath
FIG. 12 is a flowchart showing the operation of the conventional circulating bath.
[Explanation of symbols]
1 Bathtub
2 Bath water
3 Nozzle unit
4 water inlet
5 Check valve
6 Pre-filter (hair catcher)
7 Circulating water bath body
8 Circulation pipe
9 Flow sensor
10, 17a Temperature sensor
11 Circulation pump
12 Sterilizer
13 Circulation pipe
15a, 15b Circulation pipe
14 Filtration tank
16, 23, 24, 24 'three-way valve
17 Heater
18 Aluminum electrode
19 SUS electrode
20 Filter media
21 Jet nozzle
22a, 22b, 22c Circulation pipe
25 Backwash drain
26, 27 Backwash pipe
28,28 'Circulation pipe
29 Power supply
30, 30 'controller
31 Display and operation unit

Claims (7)

アルミニウム電極を有したろ過槽に浴槽水を循環させてアルミニウム電解により前記浴槽水を浄化する循環温浴器であって、前記浴槽水の循環を停止してアルミニウム電解を行うことにより前記アルミニウム電極の洗浄を行う制御部を備えていることを特徴とする循環温浴器。A circulating hot water bath for circulating bath water through a filtration tank having an aluminum electrode and purifying the bath water by aluminum electrolysis, wherein the aluminum electrode is washed by stopping the bath water circulation and washing the aluminum electrode A circulating water bath comprising a control unit for performing 前記制御部が、前記ろ過槽を加熱するろ過槽加熱手段及び/又は、前記アルミニウム電極の電解電圧の上昇を検知する電圧検知手段を備えていることを特徴とする請求項1に記載の循環温浴器。2. The circulating hot bath according to claim 1, wherein the control unit includes a filtration tank heating means for heating the filtration tank and / or a voltage detection means for detecting an increase in the electrolytic voltage of the aluminum electrode. vessel. 前記ろ過槽の下流側に設けられた三方弁が切り替えられ、循環ポンプの上流側に配設されたプレフィルター等の上流側と前記ろ過の下流側が連絡されることを特徴とする請求項1又は2に記載の循環温浴器。The three-way valve provided on the downstream side of the filtration tank is switched, and the upstream side such as a prefilter disposed on the upstream side of the circulation pump and the downstream side of the filtration are connected to each other. 2. The circulating hot water bath according to 2. アルミニウム電極を有したろ過槽に浴槽水を循環させてアルミニウム電解により前記浴槽水を浄化する循環温浴器の電極洗浄方法であって、前記ろ過槽の中の浴槽水の循環を停止させアルミニウム電解でアルミニウム電極を洗浄する電極洗浄ステップを備えていることを特徴とする循環温浴器の電極洗浄方法。An electrode cleaning method for a circulating bath that circulates bathtub water in a filtration tank having an aluminum electrode and purifies the bathtub water by aluminum electrolysis, wherein the circulation of the bathtub water in the filtration tank is stopped by aluminum electrolysis. An electrode cleaning method for a circulating warm bath characterized by comprising an electrode cleaning step for cleaning an aluminum electrode. 前記電極洗浄ステップが、ヒータで前記ろ過槽を加熱しながら行うことを特徴とする請求項4に記載の循環温浴器の電極洗浄方法。The electrode cleaning method for a circulating warm bath according to claim 4, wherein the electrode cleaning step is performed while heating the filtration tank with a heater. 前記電極洗浄ステップが、前記アルミニウム電解を停止させた後、前記ろ過槽を加熱し所定温度に加熱後アルミニウム電解を行うことを特徴とする請求項4に記載の循環温浴器の電極洗浄方法。5. The electrode cleaning method for a circulating water bath according to claim 4, wherein in the electrode cleaning step, after the aluminum electrolysis is stopped, the filtration tank is heated and heated to a predetermined temperature and then subjected to aluminum electrolysis. 前記電極洗浄ステップが、前記アルミニウム電極の電解電圧の上昇を検知した後行うことを特徴とする請求項4乃至6の内いずれか1項に記載の循環温浴器の電極洗浄方法。The method for cleaning an electrode of a circulating water bath according to any one of claims 4 to 6, wherein the electrode cleaning step is performed after detecting an increase in electrolytic voltage of the aluminum electrode.
JP27682697A 1997-10-09 1997-10-09 Circulating warm bath and electrode cleaning method Expired - Fee Related JP3775017B2 (en)

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Application Number Priority Date Filing Date Title
JP27682697A JP3775017B2 (en) 1997-10-09 1997-10-09 Circulating warm bath and electrode cleaning method

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JPH11114573A JPH11114573A (en) 1999-04-27
JP3775017B2 true JP3775017B2 (en) 2006-05-17

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