JPH11221556A - Hot bathwater circulator - Google Patents

Hot bathwater circulator

Info

Publication number
JPH11221556A
JPH11221556A JP10023403A JP2340398A JPH11221556A JP H11221556 A JPH11221556 A JP H11221556A JP 10023403 A JP10023403 A JP 10023403A JP 2340398 A JP2340398 A JP 2340398A JP H11221556 A JPH11221556 A JP H11221556A
Authority
JP
Japan
Prior art keywords
hot water
tank
bathtub
fiber membrane
hollow fiber
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
Application number
JP10023403A
Other languages
Japanese (ja)
Inventor
Yoshitaka Tsuchiya
義孝 土屋
Teruhisa Tsuruki
照久 鶴来
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Energy Support Corp
Original Assignee
Energy Support Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Energy Support Corp filed Critical Energy Support Corp
Priority to JP10023403A priority Critical patent/JPH11221556A/en
Publication of JPH11221556A publication Critical patent/JPH11221556A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Physical Water Treatments (AREA)
  • Filtration Of Liquid (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

PROBLEM TO BE SOLVED: To sterilize the pipeline of the circulator as well as hot water with a simple structure. SOLUTION: The hot water W in a bathtub Y is sucked into this hot water circulator 10, passed through a sterilization tank 13, an adsorbent tank 14 and a hollow-fiber membrane tank 16, sterilized and purified. Meanwhile, the hot water W is heated in a heat insulating tank 12 and discharged again into the bathtub Y through the circulating circuit of the circulator 10, a bypass pipe 27 is provided between the suction pipe 17 and delivery pipe 25 in the circulating circuit, and a closed circuit excluding the bathtub Y is formed. The hot water W sealed in the closed circuit is heated and circulated to sterilize the pipeline. As a result, the amt. of the hot water W heated in the heat treatment is decreased, an additional heating means is not needed, and the hot water is sufficiently heated to a specified temp. by the existing heat insulating tank 12.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、浴槽内の温水を吸
い上げて不純物を除去した後、その温水を浴槽内に吐出
する浴槽温水循環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 bath tub hot water circulating apparatus for sucking hot water in a bath tub to remove impurities and then discharging the hot water into the bath tub.

【0002】[0002]

【従来の技術】従来、浴槽温水循環装置としては、多孔
質な天然石(麦飯石等)を利用した生物化学的浄化手段
を備えたものがよく知られているが、近年ではユーザ側
の雑菌に対する意識変革により、微生物の存在自体に抵
抗感が生まれ、非生物化学的浄化が好まれる状況下にあ
る。また、浄化手段としては前記生物化学的浄化をはじ
めとし、物理的濾過等各種存在するものの各々一長一短
を有するものであった。
2. Description of the Related Art Conventionally, as a bath tub hot water circulation device, a device provided with biochemical purification means using porous natural stone (such as barley stone) has been well known. Changes in consciousness have created a feeling of resistance to the presence of microorganisms, and are now favoring non-biochemical purification. In addition, as the purifying means, there are various kinds of purifying means such as the above-mentioned biochemical purifying and physical filtration, each of which has advantages and disadvantages.

【0003】[0003]

【発明が解決しようとする課題】現在この種の浴槽温水
循環装置にあっては、浴槽水の殺菌、浄化、保温の機能
を最低限備えることが必須条件であり、且つユーザの入
浴状況、例えばスポーツ後の入浴、通常使用人数を越え
る多人数の利用等に対する急激な汚れ対応が急務といえ
る。
At present, this kind of bathtub hot water circulating apparatus is required to have at least a function of sterilizing, purifying, and keeping heat of the bathtub water, and it is necessary to provide a bathing condition of a user, for example, It is urgently necessary to take a sudden dirt response to bathing after sports and the use of many people exceeding the normal number of people.

【0004】本発明は、上記問題点を解決するために為
されたものであり、その目的は、簡単な構造にて常に安
定した浄化機能を有する浴槽温水循環装置を提供するこ
とにある。
The present invention has been made to solve the above problems, and an object of the present invention is to provide a bath tub hot water circulation device having a simple structure and always having a stable purifying function.

【0005】[0005]

【課題を解決するための手段】請求項1に記載の発明
は、ポンプにより浴槽内の温水を吸込管を介して吸い込
み、その吸い込んだ温水を保温槽及び殺菌槽を介して吸
着槽及び中空糸膜槽の順に通過させることにより濾過し
て、再度浴槽に吐出管を介して吐出する浴槽温水循環装
置において、前記温水が中空糸膜槽をバイパスして浴槽
に吐出されるバイパス回路を設けたことをその要旨とす
る。
According to the first aspect of the present invention, a hot water in a bathtub is sucked through a suction pipe by a pump, and the sucked hot water is sucked through a heat retention tank and a sterilization tank to form an adsorption tank and hollow fibers. In a bath tub hot water circulating device that filters by passing through the membrane tank in order and discharges it again to the bath tub through a discharge pipe, a bypass circuit is provided in which the hot water is discharged to the bath tub by bypassing the hollow fiber membrane tank. Is the gist.

【0006】[0006]

【発明の実施の形態】以下、本発明を具体化した一実施
形態を図1〜図4に従って説明する。浴槽温水循環装置
10は浴槽Yの上部に配置されている。そして、前記浴
槽循環装置10は、浴槽内の温水Wを吸い上げるポンプ
11, 吸い上げられた温水Wを加熱又は保温するために
ヒータを内装する保温槽12, 温水Wに紫外線を照射す
るUVランプを有する殺菌槽13, 温水Wに溶解してい
る物質を吸着する吸着剤としての多数の粒状活性炭ある
いはゼオライトの少なくとも一種類を収容した吸着剤槽
14, 温水Wに混入している固形物を濾過する中空糸膜
を収容した中空糸膜槽16等を有している。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below with reference to FIGS. The bathtub hot water circulation device 10 is disposed above the bathtub Y. The bathtub circulation device 10 has a pump 11 for sucking hot water W in the bathtub, a warming bath 12 having a heater therein for heating or keeping the drawn hot water W, and a UV lamp for irradiating the hot water W with ultraviolet rays. Sterilization tank 13, adsorbent tank 14 containing at least one kind of granular activated carbon or zeolite as an adsorbent for adsorbing substances dissolved in hot water W, hollow for filtering solids mixed in hot water W It has a hollow fiber membrane tank 16 containing a fiber membrane.

【0007】前記ポンプ11は逆止弁S及び吸込管17
を介して浴槽Y内部に接続されている。また、ポンプ1
1の上部には保温槽12及び殺菌槽13が第一連結管1
8を介して接続されており、同殺菌槽13には吸着剤槽
14が第二連結管19を介して連結されている。前記吸
着剤槽14は第三連結管20を介して五方弁15に接続
されている。即ち、前記吸着剤槽14は浴槽温水循環装
置10の内部回路に直列に配置されている。
The pump 11 has a check valve S and a suction pipe 17.
Is connected inside the bathtub Y. Pump 1
In the upper part of 1, a heat insulating tank 12 and a sterilizing tank 13 are provided with the first connecting pipe 1.
The adsorbent tank 14 is connected to the sterilization tank 13 via a second connection pipe 19. The adsorbent tank 14 is connected to a five-way valve 15 via a third connection pipe 20. That is, the adsorbent tank 14 is arranged in series with the internal circuit of the bathtub hot water circulation device 10.

【0008】前記五方弁15は第四連結管21を介して
中空糸膜槽16の上部に接続されており、同中空糸膜槽
16の下部は第五連結管22を介して再び五方弁15に
接続されている。前記五方弁15には浴槽Y内の温水W
を外部に排水するための排水管26が接続されていると
共に、同五方弁15は第六連結管23を介して三方弁2
4に接続されている。また、前記三方弁24は吐出管2
5を介して浴槽Yに接続されていると共に、バイパス管
27を介して吸込管17の途中に接続されている。
The five-way valve 15 is connected to the upper part of the hollow fiber membrane tank 16 via a fourth connection pipe 21, and the lower part of the hollow fiber membrane tank 16 is again connected to the five-way pipe via a fifth connection pipe 22. Connected to valve 15. The five-way valve 15 has hot water W in the bathtub Y.
A drain pipe 26 for draining water to the outside is connected, and the five-way valve 15 is connected to the three-way valve 2 through a sixth connection pipe 23.
4 is connected. The three-way valve 24 is connected to the discharge pipe 2
5 and connected to the bathtub Y via a bypass pipe 27 in the middle of the suction pipe 17.

【0009】尚、前記五方弁15及び三方弁24をはじ
めとする各種の構成部品間は、図示しないコントローラ
により制御されている。次に、本実施形態における通常
の浄化運転時の動作について説明する。
The various components including the five-way valve 15 and the three-way valve 24 are controlled by a controller (not shown). Next, the operation at the time of the normal purification operation in the present embodiment will be described.

【0010】図1に示すように、通常の浄化運転時に
は、前記三方弁24は第六連結管23と吐出管25とを
連結状態とする。ポンプ11が駆動されると、浴槽Y内
の温水Wは吸込管17, ポンプ11, 第一連結管18を
介して保温槽12及び殺菌槽13内に圧送される。その
後、温水Wは第二連結管19→吸着剤槽14→第三連結
管20→五方弁15→第六連結管23→三方弁24→吐
出管25の流路で浴槽Y内に吐出される。
As shown in FIG. 1, during a normal purification operation, the three-way valve 24 connects the sixth connection pipe 23 and the discharge pipe 25. When the pump 11 is driven, the hot water W in the bathtub Y is pumped into the heat retention tank 12 and the sterilization tank 13 via the suction pipe 17, the pump 11, and the first connection pipe 18. Thereafter, the hot water W is discharged into the bathtub Y through the flow path of the second connection pipe 19 → the adsorbent tank 14 → the third connection pipe 20 → the five-way valve 15 → the sixth connection pipe 23 → the three-way valve 24 → the discharge pipe 25. You.

【0011】前記保温槽12に収容されているヒータは
保温用であり、温水Wは保温槽12を通過することによ
り適温に加熱される。そして、前記温水Wは殺菌槽13
の位置を通過する際に紫外線が照射されることによって
殺菌される。紫外線による殺菌は繰り返すことでその効
果が向上するため、前記殺菌槽13は24時間稼働す
る。
The heater accommodated in the heat insulation tank 12 is used for heat insulation, and the hot water W is heated to an appropriate temperature by passing through the heat insulation tank 12. The hot water W is supplied to the sterilizing tank 13.
Are sterilized by irradiation with ultraviolet rays when passing through the position. Since the effect is improved by repeating the sterilization by ultraviolet rays, the sterilization tank 13 operates for 24 hours.

【0012】また、前記温水Wが吸着剤槽14を通過す
ることによって、同温水Wに溶解又は混入している温水
Wの濁りやヌメリの原因となるアンモニア分, タンパク
質,脂肪分等の不純物が活性炭あるいはゼオライトに吸
着されて浄化される。前記温水W中の湯垢等の非溶解性
の不純物も吸着剤槽14において物理的に濾過される。
Further, as the warm water W passes through the adsorbent tank 14, impurities such as ammonia, protein, fat, etc., which cause turbidity or slime of the warm water W dissolved or mixed in the warm water W, are removed. It is absorbed and purified by activated carbon or zeolite. Insoluble impurities such as scale in the hot water W are also physically filtered in the adsorbent tank 14.

【0013】次に、本実施形態における前記通常の浄化
運転以外の各種運転動作について説明する。まず、急速
濾過運転時の動作について説明する。
Next, various operation operations other than the normal purification operation in the present embodiment will be described. First, the operation during the rapid filtration operation will be described.

【0014】図2に示すように、急速濾過運転は、前記
コントローラによってスポーツ後の多人数入浴時等に任
意に運転される。前記急速濾過運転時には、ユーザによ
りコントローラが操作されて五方弁15が前記通常の浄
化運転から急速濾過運転に切替えられる。そして、ポン
プ11が駆動されると、浴槽Y内の温水Wは吸込管1
7, ポンプ11, 第一連結管18を介して保温槽12及
び殺菌槽13内に圧送される。その後、温水Wは第二連
結管19→吸着剤槽14→第三連結管20→五方弁15
→第四連結管21→中空糸膜槽16→第五連結管22→
五方弁15→第六連結管23→三方弁24→吐出管25
の流路で浴槽Y内に吐出される。
As shown in FIG. 2, the rapid filtration operation is arbitrarily operated by the controller when a large number of people take a bath after sports. During the rapid filtration operation, the controller is operated by the user, and the five-way valve 15 is switched from the normal purification operation to the rapid filtration operation. When the pump 11 is driven, the hot water W in the bathtub Y is supplied to the suction pipe 1.
7, pumped into the heat insulation tank 12 and the sterilization tank 13 via the first connecting pipe 18. Thereafter, the hot water W is supplied to the second connection pipe 19 → the adsorbent tank 14 → the third connection pipe 20 → the five-way valve 15
→ Fourth connecting pipe 21 → Hollow fiber membrane tank 16 → Fifth connecting pipe 22 →
Five-way valve 15 → sixth connection pipe 23 → three-way valve 24 → discharge pipe 25
Is discharged into the bathtub Y through the flow path of (1).

【0015】前記温水Wは中空糸膜槽16を通過するこ
とによって、吸着剤槽14では吸着されない固形物や各
種細菌が濾過されて急速に浄化される。尚、前記温水W
が中空糸膜槽16を通過するときの流量は5〜15 l/m
inであり流量が少ない。このため、通常、前記中空糸膜
槽16は五方弁15によってバイパスされており、急速
濾過運転は定期的に又は任意に運転される。前記浴槽Y
を四人家族が使用していると仮定した場合、急速濾過運
転を行う目安としては、一日一回の運転で通常の人の持
ち込む有機浮遊物は皆無となる。
As the hot water W passes through the hollow fiber membrane tank 16, solids and various bacteria not adsorbed in the adsorbent tank 14 are filtered and rapidly purified. The hot water W
Is 5 to 15 l / m when passing through the hollow fiber membrane tank 16.
In and the flow rate is small. For this reason, the hollow fiber membrane tank 16 is usually bypassed by the five-way valve 15, and the rapid filtration operation is performed periodically or arbitrarily. The bathtub Y
Assuming that a family of four is using, as a guideline for the rapid filtration operation, there is no organic suspended matter brought in by a normal person once a day.

【0016】前述のように、中空糸膜槽16による急速
濾過運転を繰り返すと、同中空糸膜槽16に収容されて
いる中空糸膜は徐々に目詰まりしていく。そして、前記
中空糸膜の目詰まりが進行していくと、同中空糸膜槽1
6の濾過性能が低下する。このため、中空糸膜槽16に
収容されている中空糸膜を適当な時期に洗浄する必要が
ある。本実施形態においては、通常運転時の温水Wの循
環方向とは逆方向に温水Wを循環させて中空糸膜槽16
に収容されている中空糸膜の表面に詰まった汚れを除去
する逆洗による洗浄を行う。
As described above, when the rapid filtration operation by the hollow fiber membrane tank 16 is repeated, the hollow fiber membrane contained in the hollow fiber membrane tank 16 gradually becomes clogged. As the clogging of the hollow fiber membrane progresses, the hollow fiber membrane tank 1
The filtration performance of No. 6 decreases. For this reason, it is necessary to wash the hollow fiber membrane contained in the hollow fiber membrane tank 16 at an appropriate time. In the present embodiment, the hot water W is circulated in a direction opposite to the circulation direction of the hot water W during the normal operation, so that the hollow fiber membrane tank 16
Washing by backwashing to remove dirt clogged on the surface of the hollow fiber membrane accommodated in the container.

【0017】次に、中空糸膜槽16の逆洗運転時の動作
について説明する。図3に示すように、逆洗運転時には
前記コントローラによって五方弁15が前記通常の浄化
運転時から切替わる。そして、ポンプ11が駆動される
と、浴槽Y内の温水Wは吸込管17, ポンプ11, 第一
連結管18を介して保温槽12及び殺菌槽13内に圧送
される。その後、温水Wは第二連結管19→吸着剤槽1
4→第三連結管20→五方弁15→第五連結管22→中
空糸膜槽16→第四連結管21→五方弁15→排水管2
6の流路で浴槽温水循環装置10の外部に排水される。
前記逆洗運転を行う目安としては、前述の濾過運転と同
様である。
Next, the operation of the hollow fiber membrane tank 16 during the backwash operation will be described. As shown in FIG. 3, during the backwash operation, the controller switches the five-way valve 15 from the normal cleaning operation. Then, when the pump 11 is driven, the hot water W in the bathtub Y is pumped into the heat retention tank 12 and the sterilization tank 13 via the suction pipe 17, the pump 11, and the first connection pipe 18. Thereafter, the hot water W is supplied to the second connecting pipe 19 → adsorbent tank 1
4 → third connecting pipe 20 → five way valve 15 → fifth connecting pipe 22 → hollow fiber membrane tank 16 → fourth connecting pipe 21 → five way valve 15 → drain pipe 2
The water is drained out of the bathtub hot water circulation device 10 through the flow path 6.
The standard for performing the backwashing operation is the same as the above-described filtration operation.

【0018】次に、熱処理運転時の動作について説明す
る。前述のように、通常の浄化運転, 急速濾過運転の繰
り返しにより、浴槽温水循環装置10の配管系内面や中
空糸膜槽16内部等に細菌等の微生物の繁殖が開始され
る。前記微生物は中空糸膜槽16に収容されている中空
糸膜の目詰まりを加速させてしまい、同中空糸膜の寿命
を縮める。このため、前記浴槽温水循環装置10の配管
系の内面等を殺菌し微生物の発生を防止する必要があ
る。本実施形態においては熱水を前記配管系に循環させ
ることによって微生物を殺菌する。
Next, the operation during the heat treatment operation will be described. As described above, the repetition of the normal purification operation and the rapid filtration operation causes the propagation of microorganisms such as bacteria on the inner surface of the piping system of the bath tub hot water circulation device 10 and the inside of the hollow fiber membrane tank 16. The microorganisms accelerate the clogging of the hollow fiber membrane accommodated in the hollow fiber membrane tank 16 and shorten the life of the hollow fiber membrane. For this reason, it is necessary to sterilize the inner surface of the piping system of the bathtub hot water circulation device 10 to prevent the generation of microorganisms. In this embodiment, microorganisms are sterilized by circulating hot water through the piping system.

【0019】図4に示すように、熱処理運転時には前記
コントローラによって五方弁15及び三方弁24が閉回
路Hを構成するように切替わり、同閉回路H内には温水
Wが閉じこめられる。そして、ポンプ11が駆動される
と、前記温水Wはバイパス管27→ポンプ11→第一連
結管18→保温槽12→殺菌槽13→第二連結管19→
吸着剤槽14→第三連結管20→五方弁15→第四連結
管21→中空糸膜槽16→第五連結管22→五方弁15
→第六連結管23→三方弁24→バイパス管27の流路
で浴槽Yを除く閉回路H内を循環する。本実施形態にお
いては、前記閉回路H内を循環する温水Wの量は約4 l
となっている。
As shown in FIG. 4, during the heat treatment operation, the five-way valve 15 and the three-way valve 24 are switched by the controller so as to form a closed circuit H, and the hot water W is confined in the closed circuit H. Then, when the pump 11 is driven, the hot water W flows into the bypass pipe 27 → the pump 11 → the first connecting pipe 18 → the heat retaining tank 12 → the sterilizing tank 13 → the second connecting pipe 19 →
Adsorbent tank 14 → Third connecting pipe 20 → Five-way valve 15 → Fourth connecting pipe 21 → Hollow fiber membrane tank 16 → Fifth connecting pipe 22 → Five-way valve 15
→ The sixth connecting pipe 23 → the three-way valve 24 → the bypass pipe 27 circulates in the closed circuit H except for the bathtub Y. In the present embodiment, the amount of the warm water W circulating in the closed circuit H is about 4 l.
It has become.

【0020】前記温水Wは保温槽12を通過するとによ
ってその温度が70度まで高められる。そして、前記温
水Wが閉回路Hを循環することによって、同閉回路Hの
配管内面や中空糸膜槽16に繁殖又は捕捉されている細
菌類を殺菌する。前記、温水Wは高温のため外部には排
水されず浴槽に吐出される。この際、前記温水Wの吐出
量は三方弁24によって調整され、浴槽Yに徐々に吐出
されるようになっている。
The temperature of the hot water W is raised to 70 degrees by passing through the heat retaining tank 12. Then, the warm water W circulates through the closed circuit H, thereby sterilizing bacteria that have been propagated or trapped in the pipe inner surface of the closed circuit H or the hollow fiber membrane tank 16. The hot water W is discharged to a bathtub without being drained to the outside because of the high temperature. At this time, the discharge amount of the hot water W is adjusted by the three-way valve 24 and is gradually discharged into the bathtub Y.

【0021】尚、前記熱処理運転を終了し通常運転を再
開する前に、前記コントローラにより中空糸膜槽16が
バイパスされるようになっている。即ち、第四連結管2
1,中空糸膜槽16, 第五連結管22の内部には無菌状
態の70度の温水Wが残留した状態となっている。従っ
て、中空糸膜槽16の内部は無菌状態に保持され雑菌が
繁殖しにくくなっている。また、通常運転は中空糸膜槽
16をバイパスして行われるため、雑菌が同中空糸膜槽
16の内部に入らないようになっている。
Before the heat treatment operation is completed and the normal operation is resumed, the hollow fiber membrane tank 16 is bypassed by the controller. That is, the fourth connecting pipe 2
1. Inside the hollow fiber membrane tank 16 and the fifth connecting pipe 22, sterile 70 ° C. warm water W remains. Therefore, the inside of the hollow fiber membrane tank 16 is kept in an aseptic state, and it becomes difficult for bacteria to propagate. Further, since the normal operation is performed by bypassing the hollow fiber membrane tank 16, various bacteria are prevented from entering the inside of the hollow fiber membrane tank 16.

【0022】従って、本実施形態によれば以下の効果を
得ることができる。 ・殺菌槽13を24時間稼働することにより温水Wに対
する殺菌は安定したレベルに保持できる。また、定期的
な中空糸膜槽16による急速濾過運転によって除菌、さ
らには、熱処理運転による定期的な装置10内部の配管
系路の熱殺菌にて常にシステム全体の殺菌状態が確実に
維持される。
Therefore, according to the present embodiment, the following effects can be obtained. -Sterilization of the warm water W can be maintained at a stable level by operating the sterilization tank 13 for 24 hours. In addition, the sterilization of the entire system is always maintained reliably by sterilization by the rapid filtration operation by the hollow fiber membrane tank 16 and the heat sterilization of the piping system inside the apparatus 10 by the heat treatment operation regularly. You.

【0023】・従来のように温水Wに溶解した物質に対
しては、微生物を利用した生物化学的浄化方法を採用す
ることなく吸着剤による浄化方法を採用している。これ
により、近年の生物化学的浄化離れに対する浄化手段の
代替えを可能としている。
For a substance dissolved in warm water W as in the past, a purification method using an adsorbent is employed without employing a biochemical purification method utilizing microorganisms. As a result, it is possible to substitute a purifying means for recent biochemical purification.

【0024】・ユーザの実使用に応じ、スポーツ後ある
いは多人数入浴等の通常利用と異なる場合であれ、中空
糸膜槽16による濾過機能を利用することにより、急速
濾過を可能としている。例えば、物理濾過方式として砂
濾過方式も考えられるが、急速な濾過には機能しにく
く、また、管路内への砂の流れ込み対策等が必要となり
構造上複雑となる。
According to the actual use of the user, even if it is different from normal use such as after sports or bathing for a large number of people, rapid filtration is enabled by using the filtration function of the hollow fiber membrane tank 16. For example, a sand filtration method can be considered as a physical filtration method, but it is difficult to function for rapid filtration, and it is necessary to take measures against sand flowing into a pipe, and the structure is complicated.

【0025】・常時の濾過に対し、高価で且つ目詰まり
が早い中空糸膜槽16を使用していないため、中空糸膜
の寿命を向上させることができる。尚、本実施形態は以
下のように変更して実施してもよい。
Since the expensive and quickly clogged hollow fiber membrane tank 16 is not used for regular filtration, the life of the hollow fiber membrane can be improved. Note that the present embodiment may be modified and implemented as follows.

【0026】・本実施形態では、吸着剤槽14を殺菌槽
13と五方弁15との間に配置したが、浴槽Yとポンプ
11との間、ポンプ11と保温槽12との間、五方弁1
5と三方弁24との間のいずれに配置してもよい。この
ようにしても、浴槽温水循環装置10内を循環する温水
Wの流量が十分とれ、前記実施形態と同様の効果を得る
ことができる。
In the present embodiment, the adsorbent tank 14 is disposed between the sterilizing tank 13 and the five-way valve 15, but the adsorbent tank 14 is disposed between the bath Y and the pump 11 and between the pump 11 and the heat retaining tank 12. One-way valve 1
5 and the three-way valve 24. Also in this case, a sufficient flow rate of the hot water W circulating in the bathtub hot water circulation device 10 can be obtained, and the same effect as in the above embodiment can be obtained.

【0027】・本実施形態では各種の構成部品間は、図
示しないコントローラによって自動切換されるように構
成したが、装置使用者が手動で切換えてもよい。このよ
うにしても、前記実施形態と同様の効果を得ることがで
きる。
In the present embodiment, various components are automatically switched by a controller (not shown), but may be manually switched by a user of the apparatus. Even in this case, the same effect as in the above embodiment can be obtained.

【0028】・本実施形態における中空糸膜槽16を砂
濾過槽に置き換えてもよい。このようにしても、小さな
固形物等を濾過することができる。 ・本実施形態におけるバイパス管27とポンプ11との
間に二方弁等の温水Wの流量調整手段を設けてもよい。
このようにすれば、温水Wがポンプ11に一気に流入す
ることを防止できる。
The hollow fiber membrane tank 16 in this embodiment may be replaced with a sand filtration tank. Even in this way, small solids and the like can be filtered. In the present embodiment, a flow rate adjusting means for the hot water W such as a two-way valve may be provided between the bypass pipe 27 and the pump 11.
This prevents the hot water W from flowing into the pump 11 at once.

【0029】[0029]

【発明の効果】本発明によれば、微生物による生物化学
的浄化方法を使用することなく、保温、殺菌、浄化に優
れた浴槽温水循環装置を提供できる。
According to the present invention, it is possible to provide a bath tub hot water circulation apparatus excellent in heat retention, sterilization and purification without using a biochemical purification method using microorganisms.

【図面の簡単な説明】[Brief description of the drawings]

【図1】通常浄化運転時の温水流路を示す浴槽温水循環
装置の回路図。
FIG. 1 is a circuit diagram of a bath tub hot water circulation device showing a hot water flow path during a normal purification operation.

【図2】急速濾過運転時の温水流路を示す浴槽温水循環
装置の回路図。
FIG. 2 is a circuit diagram of a bath tub hot water circulation device showing a hot water flow path during a rapid filtration operation.

【図3】逆洗運転時の温水流路を示す浴槽温水循環装置
の回路図。
FIG. 3 is a circuit diagram of a bath tub hot water circulation device showing a hot water flow path during a backwash operation.

【図4】熱処理運転時の温水流路を示す浴槽温水循環装
置の回路図。
FIG. 4 is a circuit diagram of a bath tub hot water circulation device showing a hot water flow path during a heat treatment operation.

【符号の説明】[Explanation of symbols]

10…浴槽温水循環装置、11…ポンプ、14…吸着剤
槽、15…五方弁、16…中空糸膜を収容した中空糸膜
槽、17…吸込管、25…吐出管、27…バイパス管、
H…閉回路、W…温水、Y…浴槽。
DESCRIPTION OF SYMBOLS 10 ... Hot water circulation apparatus, 11 ... Pump, 14 ... Adsorbent tank, 15 ... Five-way valve, 16 ... Hollow fiber membrane tank containing hollow fiber membrane, 17 ... Suction pipe, 25 ... Discharge pipe, 27 ... Bypass pipe ,
H: closed circuit, W: hot water, Y: bathtub.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ポンプにより浴槽内の温水を吸込管を介
して吸い込み、その吸い込んだ温水を保温槽及び殺菌槽
を介して吸着槽及び中空糸膜槽の順に通過させることに
より濾過して、再度浴槽に吐出管を介して吐出する浴槽
温水循環装置において、 前記温水が中空糸膜槽をバイパスして浴槽に吐出される
バイパス回路を設けた浴槽温水循環装置。
1. A hot water in a bathtub is sucked through a suction pipe by a pump, and the sucked hot water is filtered by passing through a heat retaining tank and a sterilizing tank in order of an adsorption tank and a hollow fiber membrane tank. A bathtub hot water circulation device for discharging water to a bathtub through a discharge pipe, wherein the hot water bypasses the hollow fiber membrane tank and is discharged to the bathtub.
JP10023403A 1998-02-04 1998-02-04 Hot bathwater circulator Pending JPH11221556A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10023403A JPH11221556A (en) 1998-02-04 1998-02-04 Hot bathwater circulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10023403A JPH11221556A (en) 1998-02-04 1998-02-04 Hot bathwater circulator

Publications (1)

Publication Number Publication Date
JPH11221556A true JPH11221556A (en) 1999-08-17

Family

ID=12109549

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10023403A Pending JPH11221556A (en) 1998-02-04 1998-02-04 Hot bathwater circulator

Country Status (1)

Country Link
JP (1) JPH11221556A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006016564A1 (en) 2004-08-11 2006-02-16 Miz Co., Ltd. Performance maintaining method in electrolysis functional water producing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006016564A1 (en) 2004-08-11 2006-02-16 Miz Co., Ltd. Performance maintaining method in electrolysis functional water producing device

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