JP2744395B2 - Water purification equipment - Google Patents

Water purification equipment

Info

Publication number
JP2744395B2
JP2744395B2 JP3054293A JP3054293A JP2744395B2 JP 2744395 B2 JP2744395 B2 JP 2744395B2 JP 3054293 A JP3054293 A JP 3054293A JP 3054293 A JP3054293 A JP 3054293A JP 2744395 B2 JP2744395 B2 JP 2744395B2
Authority
JP
Japan
Prior art keywords
water
adsorbent
tank
raw water
signal
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.)
Expired - Fee Related
Application number
JP3054293A
Other languages
Japanese (ja)
Other versions
JPH06238264A (en
Inventor
元春 佐藤
隆明 須賀
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.)
Sanden Holdings Corp
Original Assignee
Sanden 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 Sanden Corp filed Critical Sanden Corp
Priority to JP3054293A priority Critical patent/JP2744395B2/en
Publication of JPH06238264A publication Critical patent/JPH06238264A/en
Application granted granted Critical
Publication of JP2744395B2 publication Critical patent/JP2744395B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Water Treatment By Sorption (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、水道水や地下水等の原
水を一般家庭用及び業務用の飲料水として供給する浄水
装置等の水処理槽に好適で、吸着浄化能力の低下した吸
着剤を再生する装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is suitable for a water treatment tank such as a water purification device for supplying raw water such as tap water and groundwater as drinking water for general household use and business use, and has an adsorbent having reduced adsorption purification ability. To a device for playing back.

【0002】[0002]

【従来の技術】一般に、水処理装置としての浄水装置で
は、水道水や地下水等の原水に含まれる次亜塩素酸(C
lO)や有機塩素系化合物などの残留塩素成分、かび
臭、トリハロメタン、或いは一般雑菌や色素は活性炭な
どによる吸着剤で吸着除去される。経時使用によって、
活性炭及びその収納槽壁面にはこうして吸着された吸着
物質によって、藻類、細菌や微生物が繁殖するため、フ
ィルタの負荷が増したり、装置寿命を低下させたりす
る。活性炭は吸着物質によってその機能が低下するた
め、吸着物質を脱離して活性炭の再生を図り、また種々
の殺菌手段を装置に組み込むことで、浄水効率の向上、
装置のメンテナンスや保全に対応している。
2. Description of the Related Art Generally, in a water purification device as a water treatment device, hypochlorous acid (C) contained in raw water such as tap water and groundwater is used.
Residual chlorine components such as lO ) and organic chlorine-based compounds, musty odor, trihalomethane, general bacteria and pigments are adsorbed and removed by an adsorbent such as activated carbon. By use over time,
By activated carbon and adsorbent material thus adsorbed on the containing recess walls, algae, because the bacteria and microorganisms to breed, or to increase the load of the filter, or lowering the device life. Since the function of activated carbon is reduced by the adsorbed substance, the adsorbed substance is desorbed to regenerate the activated carbon, and by incorporating various sterilization means into the device, the water purification efficiency is improved.
It supports equipment maintenance and maintenance.

【0003】[0003]

【発明が解決しようとする課題】ところで、活性炭の吸
着能力が低下したこと、或いは能力が低下する時期を的
確に判断して、機能回復すべく再生処置をとることは、
活性炭はもとより装置自体の長寿命化につながるもので
あり、しかもその判定と再生の各手段は極力簡便である
ことが望ましい。
By the way, it is necessary to accurately determine when the adsorption capacity of activated carbon has decreased or when the ability has decreased, and to take a regeneration treatment to restore the function.
Activated carbon, of course, leads to a prolonged life of the apparatus itself, and it is desirable that each means for determination and regeneration be as simple as possible.

【0004】本発明の目的は、吸着能力の低下時期を経
験から設定して、吸着剤の再生を好適なインターバルで
簡便に行うことで、吸着剤はもとより装置自体の耐久性
を高めることができる浄水装置を提供することにある。
[0004] An object of the present invention is to set the timing of the decrease in the adsorption capacity based on experience, and to easily regenerate the adsorbent at suitable intervals, thereby improving the durability of the apparatus itself as well as the adsorbent. It is to provide a water purification device.

【0005】[0005]

【課題を解決するための手段】この目的を達成するた
め、本発明による浄水装置は、請求項1では、電圧を印
加すると自己発熱する吸着剤に原水を接触させる槽と、
吸着剤に接触または埋没して電圧を印加する一対の電極
と、吸着剤との接触により浄化された処理水の累積量が
設定量または設定時間を越えたことを検出する流量検出
手段と、流量検出手段からの検出信号が出力されたとき
電極間に電圧を印加する制御信号を送出する制御装置と
を備えたものである。
To achieve this object, a water purifier according to the present invention is characterized in that, in claim 1, a voltage is applied.
A tank that brings raw water into contact with the adsorbent that generates heat when added ,
A pair of electrodes for applying a voltage by contacting or immersing in the adsorbent; flow rate detecting means for detecting that the accumulated amount of treated water purified by contact with the adsorbent exceeds a set amount or a set time; And a control device for transmitting a control signal for applying a voltage between the electrodes when a detection signal is output from the detection means.

【0006】請求項2では、処理水を吸引して吐出する
ポンプを設け、ポンプから吐出される処理水の累積量が
設定量を越えたことを流量検出手段によって検出し、検
出信号に基づいて制御装置からポンプの運転を停止させ
るオフ信号を送出すると共に、電極間に電圧を印加する
制御信号を送出する構成も可能である。
According to a second aspect of the present invention, a pump for sucking and discharging the treated water is provided, and when the accumulated amount of the treated water discharged from the pump exceeds a set amount, it is detected by the flow rate detecting means and based on the detection signal. It is also possible to have a configuration in which an off signal for stopping the operation of the pump is transmitted from the control device and a control signal for applying a voltage between the electrodes is transmitted.

【0007】請求項3では、原水の通過可能な外周側フ
ィルタ及び内周側フィルタからなる二重筒体中に吸着剤
を収容したフィルタ部材を槽の内部に軸線を垂直方向に
合わせて配置し、内周側フィルタの内側貯水部に処理水
を収容する構成である。
According to a third aspect of the present invention, a filter member containing an adsorbent in a double cylindrical body comprising an outer filter and an inner filter through which raw water can pass is disposed in the tank so that its axis is vertically aligned. In this configuration, the treated water is stored in the inner water storage section of the inner peripheral filter.

【0008】請求項4では、電極が二重筒体のフィルタ
部材の上下開口部を閉塞する輪環状に成形されて吸着剤
に接触可能であるように構成することができる。
According to a fourth aspect of the present invention, the electrode can be formed in a ring shape to close the upper and lower openings of the double cylindrical filter member so that the electrode can contact the adsorbent.

【0009】請求項5では、再生信号の送出前に貯水部
を含む槽内全域から原水を排水して抜き取る構成であ
る。
According to a fifth aspect of the present invention, the raw water is drained and extracted from the entire area of the tank including the water storage section before the reproduction signal is transmitted.

【0010】請求項6では、槽内に原水を導入する導入
管に切換弁を設け、制御装置からの切換信号による切換
弁の切り替えで貯水部を含む槽内全域から原水を排水し
て抜き取る構成も可能である。
According to a sixth aspect of the present invention, a switching valve is provided in an introduction pipe for introducing raw water into the tank, and the switching valve is switched by a switching signal from a control device to drain and drain raw water from the entire area including the water storage section. Is also possible.

【0011】請求項7では、吸着剤中に温度検出手段を
配し、吸着剤の温度が設定温度を越えたことの検出信号
に基づいて電極にオフ信号を送出して電圧印加を停止す
ることもできる。
According to a seventh aspect of the present invention, a temperature detecting means is provided in the adsorbent, and an off signal is sent to the electrode based on a detection signal indicating that the temperature of the adsorbent has exceeded a set temperature to stop voltage application. Can also.

【0012】[0012]

【作用】請求項1の場合、流量検出手段によって浄化済
み処理水の累積量が設定量を越えたことを検出して、こ
の検出信号に基づいて制御装置から電極に電圧を印加し
て吸着剤に吸着した物質を脱離させる。処理水の累積
が設定量に達したかどうか管理することで、吸着剤の再
生時期をインターバル化できる。処理水の槽からの注出
は、供給源から原水を圧送する水圧による押し出しで可
能である。
In the case of the first aspect, the flow rate detecting means detects that the accumulated amount of the purified treated water exceeds the set amount, and applies a voltage to the electrode from the control device based on the detected signal to thereby adsorb the adsorbent. The substance adsorbed on the substrate is desorbed. By managing whether the accumulated amount of the treated water has reached the set amount, the regeneration time of the adsorbent can be set as an interval. Discharge of the treated water from the tank can be achieved by water pressure extruding raw water from a supply source.

【0013】請求項2の場合、請求項1でいう原水供給
源の水圧利用に代えて、例えば自給式のポンプを設け、
ポンプから吐出される処理水の累積量が設定量を越えた
ことを流量検出手段によって検出するものである。
In the case of claim 2, for example, a self-contained pump is provided instead of using the water pressure of the raw water supply source according to claim 1.
The flow rate detecting means detects that the accumulated amount of the treated water discharged from the pump exceeds the set amount.

【0014】請求項3〜6の場合、再生信号の送出前
に、二重筒体のフィルタ部材の貯水部を含む槽内全域か
ら原水を排水し、吸着剤から原水を抜き取って電圧印加
すると、吸着物質の脱離がさらに効率的である。
In the case of claim 3 to claim 6, before sending out the reproduction signal, if the raw water is drained from the entire area including the water storage part of the double cylindrical filter member, the raw water is extracted from the adsorbent and a voltage is applied, Desorption of the adsorbed material is more efficient.

【0015】請求項7では、電圧印加による吸着剤の加
熱時に、吸着剤の温度を検出することで、設定温度を越
えた場合は電極にオフ信号を送出して電圧印加を停止で
き、電源コントロールで消費電力の節減が可能になる。
According to a seventh aspect of the present invention, when the adsorbent is heated by applying a voltage, the temperature of the adsorbent is detected, and when the temperature exceeds a set temperature, an off signal is sent to the electrode to stop the voltage application, thereby enabling power supply control. Thus, power consumption can be reduced.

【0016】[0016]

【実施例】以下、本発明による浄水装置の実施例を図面
に基づいて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the water purification apparatus according to the present invention will be described below with reference to the drawings.

【0017】図1は、実施例の浄水装置の断面図であ
る。全体が円筒形に成形された本体槽10には、浄化処
理される原水として例えば水道水が供給水源から導入口
11を通して導入される。この導入口11は排水管路も
兼用していて、原水の導入または排水に切り替えるため
の電磁弁による三方向切換弁(三方弁)12が設けてあ
る。三方弁12は切換信号により動作して原水を本体槽
10内に導入する場合と、また逆に本発明の主旨である
吸着剤再生時は本体槽10内に残留原水を排水して空に
する場合の給排水両機能用に設定してある。
FIG. 1 is a sectional view of a water purification apparatus according to an embodiment. For example, tap water is introduced from a supply water source through the inlet 11 as raw water to be purified into the main body tank 10 which is entirely formed into a cylindrical shape. The inlet 11 also serves as a drainage pipe, and is provided with a three-way switching valve (three-way valve) 12 using an electromagnetic valve for switching to introduction or drainage of raw water. The three-way valve 12 operates in response to a switching signal to introduce raw water into the main body tank 10, and conversely, during regeneration of the adsorbent which is the gist of the present invention, drains residual raw water into the main body tank 10 to empty it. It is set for both functions of water supply and drainage in case.

【0018】本体槽10内には二重筒体のフィルタ部材
20が軸線を垂直方向に平行に収納されている。フィル
タ部材20は原水の通過が可能な外周側フィルタ21及
び内周側フィルタ22からなっていて、両フィルタ間の
ドーナツ状空間に吸着剤の活性炭23が充填されてい
る。本発明でいう吸着剤は導電性の発熱体であって、
圧を印加すると自己発熱するものであり、この性質を有
するものであれば、使用吸着剤として活性炭23に限定
されない。また、図1で明らかなように、本体槽10と
内周面との間には外周側フィルタ21に沿って環状の空
間部24が生じるように部材のサイズを設定してあり、
原水導入口11から本体槽10内に導入された水道水は
空隙部24を周回して外側フィルタ21を通り内部の活
性炭23に接触可能である。活性炭23を通過して浄化
処理された水道水は内周側フィルタ22の内側、つまり
フィルタ部材20の中央の空間部を貯水部29としてこ
こにいったん導出するようになっている。
A double cylindrical filter member 20 is accommodated in the main body tank 10 with its axis parallel to the vertical direction. The filter member 20 includes an outer filter 21 and an inner filter 22 through which raw water can pass, and a donut-shaped space between both filters is filled with activated carbon 23 as an adsorbent. Adsorbent in the present invention is a conductive heating element, electrostatic
Self-heating when pressure is applied.
If it does , the used adsorbent is not limited to activated carbon 23. As is clear from FIG. 1, the size of the member is set so that an annular space 24 is formed between the main body tank 10 and the inner peripheral surface along the outer peripheral filter 21.
Tap water introduced from the raw water introduction port 11 into the main body tank 10 circulates around the gap 24, passes through the outer filter 21, and can contact the activated carbon 23 inside. Tap water that has been purified by passing through the activated carbon 23 is once drawn out of the inner peripheral filter 22, that is, the central space of the filter member 20 as a water reservoir 29.

【0019】また、図2〜図5に示すように、二重筒体
のフィルタ部材20の上下開口部はドーナツ円盤形に成
形された一対の電極25,26の嵌合によって閉塞され
ている。電極25,26にはそれぞれ端子25a,26
aが設けられ、本体槽10の外部に突出して電気配線に
備えている。また、電極25,26の内面にはそれぞれ
数個の凸部25b,26bが設けてあり、これらは活性
炭23中に埋没させて接触を確実なものにすると同時
に、フィルタ部材20に対して電極25,26を位置決
めする機能がある。活性炭23を収容したフィルタ部材
20と電極25,26は下方から取付板27によって支
持されている。図4及び図5に示すように、取付板27
は本体槽10の内周に嵌合する円板で、下方に原水導入
または排水に備えて空間部13を設けて固定されてい
る。また、取付板27の外周部には原水を通せる多数の
通し孔27aが設けてあり、空間部13の原水を通し孔
27aからフィルタ部材20の外周側の空隙部24に導
入可能となっている。排水時は逆に空隙部24から下方
の空間部13へ排出される。通し孔27aに重ねて輪状
のプレフィルタ28が設けられ、原水を活性炭23に接
触させる前にろ過するようになっている。
As shown in FIGS. 2 to 5, the upper and lower openings of the double cylindrical filter member 20 are closed by fitting a pair of electrodes 25 and 26 formed into a donut disk shape. The electrodes 25 and 26 have terminals 25a and 26, respectively.
a is provided and protrudes out of the main body tank 10 to prepare for electric wiring. Also, several convex portions 25b, 26b are provided on the inner surfaces of the electrodes 25, 26, respectively. These are buried in the activated carbon 23 to ensure contact, and at the same time, the electrodes 25, 26 , 26 are positioned. The filter member 20 containing the activated carbon 23 and the electrodes 25 and 26 are supported by a mounting plate 27 from below. As shown in FIG. 4 and FIG.
Is a disk fitted into the inner periphery of the main body tank 10 and provided with a space 13 below for preparation of raw water introduction or drainage and fixed. A large number of through holes 27 a through which raw water can pass are provided in the outer peripheral portion of the mounting plate 27, and the raw water in the space 13 can be introduced from the through hole 27 a into the gap 24 on the outer peripheral side of the filter member 20. I have. On the contrary, at the time of drainage, the water is discharged from the space 24 to the space 13 below. A ring-shaped pre-filter 28 is provided so as to overlap with the through hole 27 a, and is configured to filter raw water before it comes into contact with the activated carbon 23.

【0020】一方、フィルタ部材20の内周側フィルタ
22の内側空間にはUVランプ(殺菌手段)30が配置
され、UVランプ30への通電による照射紫外線で活性
炭23を通過した原水を更に殺菌するようになってい
る。また、UVランプ30に並んでオゾン導入管31が
導入され、図示しないオゾン発生器からオゾン導入管3
1を通してオゾン(O)を供給可能であり、UVラン
プ30の紫外線による殺菌とともに、オゾンでも殺菌効
果を高めている。
On the other hand, a UV lamp (sterilizing means) 30 is disposed in the inner space of the inner peripheral side filter 22 of the filter member 20, and the raw water passing through the activated carbon 23 is further sterilized by ultraviolet rays irradiated by energizing the UV lamp 30. It has become. Further, an ozone introduction pipe 31 is introduced alongside the UV lamp 30, and an ozone generator 3 (not shown) supplies an ozone introduction pipe 3.
Ozone (O 3 ) can be supplied through 1, and the sterilizing effect of the ozone is enhanced by the ozone as well as the sterilization by the UV light of the UV lamp 30.

【0021】UVランプ30及びオゾン導入管31に並
んで、内周側フィルタ22の内側空間には浄化殺菌処理
された原水を使用に供するためにくみ出すための自給式
ポンプ32の吸入管33を臨ませている。自給式ポンプ
32の吐出管34にはポンプ吐出量を検出する流量検出
器(手段)36が設けられ、ポンプ吐出量が積算設定量
(処理水の累積量)を越えたとき、これを検出して信号
を図6で示す制御装置40に送出するようになってい
る。吐出管34には電磁弁による三方向切換弁35が設
けられ、この切換弁35にはドレン管37も切換可能に
接続されている。
Along with the UV lamp 30 and the ozone introduction pipe 31, an intake pipe 33 of a self-contained pump 32 for pumping raw water that has been purified and sterilized for use in the inner space of the inner peripheral filter 22 is provided. I'm facing. The discharge pipe 34 of the self-contained pump 32 is provided with a flow detector (means) 36 for detecting the pump discharge amount.
When it exceeds (accumulated amount of treated water) , this is detected and a signal is sent to the control device 40 shown in FIG. The discharge pipe 34 is provided with a three-way switching valve 35 using an electromagnetic valve, and a drain pipe 37 is also connected to the switching valve 35 so as to be switchable.

【0022】但し、実施例では処理水のくみ出しに自給
式ポンプ32が用いられたが、原水の供給源からの供給
水圧を利用して処理水を本体槽10から注出させること
もできる。この場合は、自給式ポンプ32は不要であ
り、また、処理水を使用時に出す注出管路の好適場所に
流量検出器36を配置しておけばよい。
In the embodiment, the self-contained pump 32 is used for extracting the treated water. However, the treated water can be discharged from the main tank 10 by using the pressure of the raw water supplied from the supply source. In this case , the self-contained pump 32 is unnecessary.
In addition, the flow rate detector 36 may be arranged at a suitable place of the discharge pipe for discharging the treated water at the time of use.

【0023】また、実施例では流量検出器36でポンプ
吐出量の設定積算量を管理しているが、経験的に吐出量
が時間の経過で一定と想定できるならば、設定流量に等
価の設定時間をタイマーの計測により管理することも可
能である。また、殺菌機能を必要とせず浄水機能のみを
必要とする場合は、UVランプやオゾン導入管を削除す
ることによってより小型にすることも可能である。
Further, in the embodiment, the set integrated amount of the pump discharge amount is managed by the flow rate detector 36. However, if the discharge amount can be empirically assumed to be constant over time, a setting equivalent to the set flow amount is set. It is also possible to manage the time by measuring a timer. When only the water purification function is required without the need for the sterilization function, the size can be further reduced by removing the UV lamp and the ozone introduction tube.

【0024】図6に示す制御回路のブロック図におい
て、マイクロコンピュータ等による制御装置40は中央
演算装置(CPU)41、メモリ42及びI/Oポート
43等から構成され、流量検出器35及び作動投入スイ
ッチ38からI/Oポート43に入力された検出信号に
よってメモリ42に記憶されているプログラムに基づい
て制御が行われ、制御信号をI/Oポート43から制御
対象の外部機器、即ち自給式ポンプ32、吐出管34の
切換弁35、一対の電極25,26、UVランプ30、
そしてオゾン導入管31にオゾンを供給する発生器等に
オンオフ信号を送出するようになっている。
In the block diagram of the control circuit shown in FIG. 6, a control unit 40 such as a microcomputer comprises a central processing unit (CPU) 41, a memory 42, an I / O port 43, etc., a flow rate detector 35 and an operation input. Control is performed based on a program stored in the memory 42 by a detection signal input from the switch 38 to the I / O port 43, and a control signal is transmitted from the I / O port 43 to an external device to be controlled, that is, a self-contained pump. 32, a switching valve 35 of a discharge pipe 34, a pair of electrodes 25 and 26, a UV lamp 30,
Then, an on / off signal is sent to a generator or the like that supplies ozone to the ozone introduction pipe 31.

【0025】次に、以上の構成による実施例の動作態様
及び作用を図7のフローチャートと、図8及び図9のタ
イムチャートを併用して説明する。
Next, the operation mode and operation of the embodiment having the above configuration will be described with reference to the flowchart of FIG. 7 and the time charts of FIGS. 8 and 9.

【0026】通常使用時は、制御装置40からの切換信
号で切換弁12が切り替えられ、処理用原水である例え
ば水道水が導入口11から本体槽10内に導入される
(ステップS)。水道水は下部空間部13から取付板
27の通し孔27aを通り、プレフィルタ28でろ過さ
れてフィルタ部材20の周囲空隙部24に入る。水道水
はここから外周側フィルタ21を通過して活性炭23に
接触し、浄化されて内周側フィルタ22を通って中央の
貯水部29に導入される。活性炭23への接触によって
水道水に含まれた溶存物質、例えば微量有機塩素化合
物、微量有機化合物やかび臭の発生原因物質であるジオ
スミン、2メチルイソボルネオール等が吸着除去される
(ステップS)。
During normal use, the switching valve 12 is switched by a switching signal from the control device 40, and raw water for processing, for example, tap water, is introduced into the main tank 10 from the inlet 11 (step S 1 ). Tap water passes through the through hole 27 a of the mounting plate 27 from the lower space 13, is filtered by the pre-filter 28, and enters the surrounding space 24 of the filter member 20. From here, the tap water passes through the outer filter 21, comes into contact with the activated carbon 23, is purified, and is introduced into the central water storage 29 through the inner filter 22. Dissolved substance contained in tap water by contact with activated carbon 23, such trace organic chlorine compounds, diosmin is a cause material of trace organic compounds and musty, like 2-methyl-isoborneol is adsorbed and removed (step S 2).

【0027】貯水部29が処理水でほぼ満杯になったタ
イミングをみて、装置を立ち上げる投入スイッチ38の
操作で自給式ポンプ32が運転開始し、同時に吐出管3
4の切換弁35を作動させて使用時の注出に備える。こ
のときUVランプ30にも制御装置40からオン信号が
送られていて、オゾン導入管31を通してオゾン発生器
からオゾンが中央貯水部29の処理水に供給されて混入
する。即ち、溶存物質が取り除かれ中央空間部に導入さ
れた浄化処理水には、UVランプ30からの紫外線が照
射され、オゾン導入管31からオゾンを供給して混入さ
せる。これによって処理水の細菌類を殺菌し、藻類、有
機化合物及び無機化合物等を酸化分解する(ステップS
)。こうして浄化、殺菌された処理水は吸入管33を
通して自給式ポンプ32に吸引され、吐出管34から吐
出されて使用時の注出に備え、飲料水等に供される(ス
テップS)。
At the timing when the water storage section 29 is almost full of the treated water, the self-contained pump 32 is started to operate by operating the input switch 38 for starting the apparatus, and at the same time, the discharge pipe 3 is turned on.
The switching valve 35 of No. 4 is operated to prepare for pouring during use. At this time, an ON signal is also sent from the control device 40 to the UV lamp 30, and ozone is supplied from the ozone generator to the treated water in the central water storage unit 29 through the ozone introduction pipe 31 and mixed therein. That is, ultraviolet light from the UV lamp 30 is applied to the purified water that has been removed and introduced into the central space after the dissolved substances have been removed, and ozone is supplied from the ozone introduction pipe 31 and mixed therein. Thereby, bacteria in the treated water are sterilized, and algae, organic compounds, inorganic compounds, and the like are oxidatively decomposed (step S).
3 ). Thus purified, sterilized treated water is sucked into the self-contained pump 32 through the suction pipe 33, discharged from the discharge pipe 34 provided to dispense in use, it is subjected to water or the like (step S 4).

【0028】一方、経時使用によって、自給式ポンプ3
2のポンプ吐出量が設定積算量を越えたとき、これを吐
出管34に設けられた流量検出器36が検出し、信号を
制御装置40に送出する(ステップS)。即ち、流量
検出器36から検出信号が送出されたことで、フィルタ
部材20内の活性炭23の吸着能力が低下したと判断さ
れ、制御装置40によって次の手順により活性炭23の
機能を回復する再生処理が施される。
On the other hand, the self-contained pump 3
When the pump discharge quantity of 2 exceeds the set integration amount, which is detected by the flow detector 36 provided in the discharge pipe 34, and sends a signal to the controller 40 (step S 5). That is, since the detection signal is sent from the flow rate detector 36, it is determined that the adsorption ability of the activated carbon 23 in the filter member 20 is reduced, and the control device 40 restores the function of the activated carbon 23 in the following procedure. Is applied.

【0029】流量検出器36からの検出信号に基づい
て、制御装置40では再生を促す警報もしくは表示信号
などを出すと同時に、自給式ポンプ32の運転、UVラ
ンプ30への通電、そしてオゾン導入管31からのオゾ
ン供給をそれぞれ停止するオフ信号を送出する(ステッ
プS)。
On the basis of the detection signal from the flow rate detector 36, the control device 40 issues a warning or a display signal urging regeneration, and at the same time, operates the self-contained pump 32, energizes the UV lamp 30, and supplies the ozone introduction pipe. An off signal for stopping the supply of ozone from 31 is sent out (step S 6 ).

【0030】これにぼぼ同期して、原水導入口11側の
切換弁12に切換信号が送られ、それまでの原水導入ポ
ートを閉じ、逆に排水ポートを開いて本体槽10内の残
存水道水を排水して空状態にする。即ち、活性炭23中
にあって接触している水道水、中央貯水部29に導入さ
れた処理水もこの場合は一切排出される。排水は外周側
フィルタ21を抜けてこの外側の環状空隙部24から通
し孔27aを通し逆流させて、導入口11を排水口とし
て外部排水する(ステップS)。
Synchronously with this, a switching signal is sent to the switching valve 12 on the side of the raw water inlet 11, and the raw water introducing port up to that point is closed, and the drain port is opened to open the remaining tap water in the main tank 10. Drain and empty. That is, the tap water in the activated carbon 23 that is in contact with the treated water and the treated water introduced into the central water storage section 29 are all discharged in this case. Wastewater by reverse flow through the hole 27a through this outer annular gap portion 24 leaves the outer peripheral side filter 21, to an external drain the inlet 11 as drainage port (step S 7).

【0031】次いで、フィルタ部材20の上下に配置さ
れた両電極25,26間に電圧を印加し、活性炭23に
通電して抵抗体として加熱することにより、吸着物質が
脱離する(ステップS)。任意時間電圧を印加した
後、制御装置40から電極25,26にオフ信号が送ら
れて電圧の印加を停止する。この後、ステップSに戻
って通常使用の運転に切り替えられる(ステップ
)。
[0031] Then, a voltage is applied between the electrodes 25 and 26 disposed above and below the filter member 20, by heating the resistor by energizing the activated carbon 23, the adsorbent material is desorbed (Step S 8 ). After the voltage is applied for an arbitrary time, an off signal is sent from the control device 40 to the electrodes 25 and 26, and the application of the voltage is stopped. Thereafter, switched to normal use operation returns to the step S 2 (step S 9).

【0032】なお、以上の実施例において、フィルタ部
材20を二重筒体として、その外周回りから原水を通過
させることに次の利点がある。即ち、内周側フィルタ2
2の内側を空間にし、ここにUVランプ30等からなる
殺菌手段を配置した貯水部29としたことにより、一槽
で本体槽10の内部を浄水領域と殺菌領域に隔成して両
用できる。つまり従来この種装置が浄水槽と殺菌槽を別
々に設けた二槽タイプであるのに対して、本発明では装
置全体が簡素で小型化が可能となる。また、別の利点と
して、原水が外周領域の空隙部24を周回して外側フィ
ルタ21を通る構造としているため、活性炭23に対し
て原水の通過する表面積が一層広く増し、その結果圧力
損失が軽減される。更に別の利点としては、吸着剤とし
ての活性炭23に繊維状のものを使用することにより、
上下に配置した電極25,26による通電効率が良好で
ある。最後に利点として、活性炭23における原水の通
過表面積が大きいために、活性炭23による吸着剤層の
汚れが少なくてすみ、層の厚さを薄くできるために、排
水する際の汚れを除去し易く、洗浄効果を高めることが
できる。
In the above embodiment, the following advantage is obtained by forming the filter member 20 as a double cylindrical body and passing the raw water from around the outer periphery thereof. That is, the inner peripheral filter 2
The interior of the main tank 10 is divided into a water purification area and a sterilization area by using a single tank so that the inside of the main tank 10 can be used for both purposes. That is, while this type of apparatus has conventionally been a two-tank type in which a water purification tank and a sterilization tank are separately provided, the present invention allows the entire apparatus to be simplified and reduced in size. Another advantage is that the surface of the raw water passes through the outer filter 21 around the void 24 in the outer peripheral region, so that the surface area of the raw water that passes through the activated carbon 23 is further increased, and as a result, pressure loss is reduced. Is done. As another advantage, by using a fibrous material for the activated carbon 23 as an adsorbent,
The energization efficiency by the electrodes 25 and 26 arranged above and below is good. Finally, as an advantage, since the surface area of raw water passing through the activated carbon 23 is large, contamination of the adsorbent layer by the activated carbon 23 can be reduced, and the thickness of the layer can be reduced.
Facilitate removal of dirt when you water, it is possible to enhance the cleaning effect.

【0033】図10以下の図面は本発明の第2実施例を
示し、新設または既設の大型水槽50にセットされたフ
ロート型浄水装置60の断面図である。水槽50には、
浄化処理される原水としての例えば水道水が導入管路5
1を通し水源から導入される。フロート型浄水装置60
は水槽50内で原水に浮かんだ状態でセットされ、原水
を浄化及び殺菌した処理水は、導出口55に接続され
出弁53を備えた注出管路54から注出されて飲料水等
に供されるようになっている。水槽50の上部はマンホ
ール56で閉塞されており、マンホール56には導入管
路51に接続される原水導入口52を設けることもでき
る。
FIG. 10 and subsequent drawings show a second embodiment of the present invention, and are cross-sectional views of a float type water purifier 60 set in a new or existing large water tank 50. FIG. In the water tank 50,
For example, tap water as raw water to be purified is introduced into the introduction line 5.
1 through a water source. Float type water purifier 60
Is set in a state of being floated on raw water in a water tank 50, and treated water obtained by purifying and sterilizing the raw water is discharged from a discharge pipe 54 having a discharge valve 53 connected to an outlet 55, and drinking water, etc. It is to be offered to. The upper part of the water tank 50 is closed by a manhole 56, and the manhole 56 may be provided with a raw water inlet 52 connected to the inlet conduit 51.

【0034】既設の水槽50内にフロート型浄水槽60
を後付けで装着する場合、水槽50のマンホール56を
開き、浄水槽60全体を原水に浮かせ、所要の配管や電
気配線を行うだけで、据え付けには特別な工事を要しな
い。装置60全体は原水に浮かせることが可能な構造で
あり、搭載の自給式ポンプ61で揚水した原水を浄化及
び殺菌して再び水槽50内に戻すことができる。装置6
0の構成は、原水面に浮力で浮くことができる浮力部材
62を有し、この浮力部材62の浮力でもって内外二重
筒体の第1槽70及び第2槽80からなる本体部を原水
内に保持可能である。
The float type water purifying tank 60 is provided in the existing water tank 50.
When retrofitting is required, the manhole 56 of the water tank 50 is opened, the entire water purification tank 60 is floated on the raw water, necessary piping and electric wiring are performed, and no special construction is required for installation. The entire device 60 has a structure capable of floating in raw water, and the raw water pumped by a self-contained pump 61 mounted thereon can be purified and sterilized and returned to the water tank 50 again. Device 6
No. 0 has a buoyancy member 62 capable of floating on the raw water surface by buoyancy, and the buoyancy of the buoyancy member 62 causes the main body composed of the first and second inner and outer cylinders 70 and the second tub 80 to be removed from the raw water surface. Can be held within.

【0035】ここで、第1槽70は内部に吸着剤である
活性炭75が充填されている。第1槽70の底部71に
は水槽50内の原水を自給式ポンプ1で吸引する揚水
管72が設けられ、この揚水管72は水槽50の異なる
サイズに対応できるよう、固定管72aに対して可動管
72bを摺動させ、管長さの全長Hを調整できる。ま
た、第1槽70の上下には透水性のフィルタ73,74
が口径断面を閉塞するように設けられ、揚水管72から
導入される原水をろ過するようになっている。これら上
下のフィルタ73,74間には吸着剤、即ち前記実施例
と同様に電圧を印加すると自己発熱する活性炭75が充
填されている。
Here, the first tank 70 is filled with activated carbon 75 as an adsorbent. The bottom 71 of the first tank 70 riser pipe 72 is provided for sucking the raw water in the water tank 50 by the self-contained pump 61, the riser pipe 72 to accommodate the different sizes of the water tank 50, the fixed tube 72a By sliding the movable tube 72b, the total length H of the tube length can be adjusted. Water-permeable filters 73 and 74 are provided above and below the first tank 70.
Is provided so as to close the caliber section, and is configured to filter raw water introduced from the pumping pipe 72. An adsorbent between the upper and lower filters 73 and 74 , that is, the above-described embodiment is used.
Activated carbon 75 that self-heats when a voltage is applied in the same manner as described above.

【0036】また、第1槽70内においては、本発明の
要旨部材である吸着剤の、つまり活性炭75の再生手段
が装備されている。再生手段を構成する主要部材は一対
の電極76,76である。両電極76,76は第1槽7
0内でこの径方向両端に対極をなすようにして配置され
る。両電極76,76は同一形状に配置され、それぞれ
第1槽70の上蓋77に絶縁部材78を介して挿通した
端子棒76aを有し、端子棒76aには外部リード線が
配線されている。また、端子棒76aの下端にはステン
レス鋼製の電極板79が結合され、この電極板79は
第1槽70の内周面に沿って円弧状に成形され、大部分
は活性炭75中に没入して接触させている。円弧状に成
形することによって活性炭75との接触面積が大きくな
り有効である。このような一対の電極76,76間には
電圧が印加され、電極板79によって導電性の活性炭7
5に通電して加熱する構成である。
Further, in the first tank 70, means for regenerating the adsorbent, ie, the activated carbon 75, which is a gist of the present invention, is provided. Major members constituting the reproducing means is a pair of electrodes 76, 76. Both electrodes 76, 76 are in the first tank 7
Within 0, they are arranged so as to form opposite electrodes at both ends in the radial direction. The two electrodes 76, 76 are arranged in the same shape, each having a terminal rod 76a inserted into the upper lid 77 of the first tank 70 via an insulating member 78, and an external lead wire is wired to the terminal rod 76a. An electrode plate 79 made of stainless steel or the like is connected to the lower end of the terminal rod 76a. The electrode plate 79 is formed in an arc shape along the inner peripheral surface of the first tank 70. Immersive contact. Forming in an arc shape is effective because the contact area with the activated carbon 75 increases. A voltage is applied between the pair of electrodes 76, 76, and the conductive activated carbon 7 is
5, and the structure is heated.

【0037】一方、第1槽70内にはこの同軸上に第2
槽80が収納されている。この第2槽80は、第1槽7
0において活性炭75との接触で浄化された浄化処理水
のさらに殺菌を目的とした槽である。第2槽80は上下
を閉塞する形で透水性のフィルタ部材81,82を有
し、第1槽70からの浄化処理水をろ過して内部に導入
可能である。また、中心軸上を挿通するようにしてUV
ランプ(殺菌手段)83が配置され、UVランプ83へ
の通電による照射紫外線で浄化処理水を殺菌するように
なっている。また、UVランプ83に軸を平行にして第
2槽80内にはオゾン導入管84が導入され、図示しな
いオゾン発生器からオゾン導入管84を通してオゾン
(O)を供給可能であり、UVランプ83の紫外線に
よる殺菌とともに、オゾンでも殺菌効果を高めている。
On the other hand, in the first tank 70, the second
The tank 80 is stored. The second tank 80 includes the first tank 7
0 is a tank for the purpose of further sterilizing purified water treated by contact with activated carbon 75. The second tank 80 has water-permeable filter members 81 and 82 so as to close the upper and lower sides, and can purify the purified water from the first tank 70 and introduce it into the inside. Also, the UV light is inserted through the center axis.
A lamp (sterilizing means) 83 is disposed, and the purified water is sterilized by ultraviolet rays irradiated by energizing the UV lamp 83. An ozone introduction tube 84 is introduced into the second tank 80 with the axis parallel to the UV lamp 83, and ozone (O 3 ) can be supplied from an ozone generator (not shown) through the ozone introduction tube 84. In addition to the sterilization by 83 ultraviolet rays, ozone enhances the sterilization effect.

【0038】また、第2槽80は前述の自給式ポンプ6
1に吸入管85で配管されて接続されている。この吸入
管85は第2槽80の下部フィルタ81から第1槽70
内の活性炭75による吸着層を挿通し、槽外に出て自給
式ポンプ51の吸入側に連結されている。自給式ポンプ
61の吐出管57にはポンプ吐出量を検出する流量検出
器58が設けられ、ポンプ吐出量が積算設定量を越えた
とき、これを検出して信号を図6で示された制御装置4
0に送出するようになっている。
The second tank 80 is provided with the self-contained pump 6 described above.
1 is connected by piping through a suction pipe 85. The suction pipe 85 extends from the lower filter 81 of the second tank 80 to the first tank 70.
It is inserted through an adsorption layer made of activated carbon 75 inside, goes out of the tank, and is connected to the suction side of the self-contained pump 51. The discharge pipe 57 of the self-contained pump 61 is provided with a flow rate detector 58 for detecting the pump discharge amount. Device 4
0 is sent.

【0039】また、図13は、図11及び図12で示さ
れた実施例の電極7に代えて、構造のコンパクト化を
狙った変形例である。この場合の電極90は先端鋭利な
直線棒状に成形され、第1槽70内の活性炭75に差し
込んでセットするのみで、非常に簡単な構造ですむ。こ
うした第2実施例の場合、自給式ポンプ61の作動で水
槽50内の原水がフロート型浄水槽60の第1槽70に
下底の揚水管72から吸引される。第1槽70内の活性
炭75に対して、原水を下底の揚水管72から導入して
接触させるということは、活性炭75の下層に微生物が
まずはじめに生息することで、生物ろ過膜が生じること
になり、ろ過能力が向上する利点がある。また、揚水管
72の管長Hは水槽50の大きさに対応させて自在に調
整される。第1槽70内にフィルタ73でろ過して導入
された原水は活性炭75による吸着層に接触し、原水に
含まれた溶存物質、例えば微量有機塩素化合物、微量有
機化合物やかび臭の発生原因物質であるジオスミン、2
メチルイソボルネオール等が吸着除去される。
Further, FIG. 13, in place of the electrode 7 6 for the embodiment shown in FIGS. 11 and 12, a modification aimed compact structure. In this case, the electrode 90 is formed in the shape of a straight rod having a sharp tip, and only needs to be inserted into the activated carbon 75 in the first tank 70 and set. In the case of the second embodiment, the raw water in the water tank 50 is sucked into the first tank 70 of the float type water purification tank 60 from the lower pumping pipe 72 by the operation of the self-contained pump 61. The fact that the raw water is introduced into and brought into contact with the activated carbon 75 in the first tank 70 from the lower bottom pumping pipe 72 means that microorganisms first inhabit the lower layer of the activated carbon 75, thereby forming a biological filtration membrane. And there is an advantage that the filtration capacity is improved. Further, the pipe length H of the pumping pipe 72 is freely adjusted according to the size of the water tank 50. The raw water introduced into the first tank 70 after being filtered by the filter 73 comes into contact with the adsorption layer formed by the activated carbon 75, and is a dissolved substance contained in the raw water, for example, a trace organic chlorine compound, a trace organic compound, or a substance causing mold odor. A geosmin, 2
Methyl isoborneol and the like are adsorbed and removed.

【0040】原水から溶存物質が取り除かれた浄化処理
水は、次いで第2槽80内にフィルタ81,82でろ過
されて導入される。導入された浄化処理水にはUVラン
プ83からの紫外線が照射され、オゾン導入管84を通
しオゾン発生器からオゾンも供給される。これによって
浄化処理水の細菌類を殺菌し、藻類、有機化合物及び無
機化合物等を酸化分解する。こうして浄化、殺菌された
処理済み水は吸入管85を通して自給式ポンプ61に吸
引され、吐出管57の先端から吐出して水槽50内に戻
される。原水の揚水と浄化殺菌と戻しの循環を繰り返
し、水槽50内の浄化殺菌処理水を使用時は注出53
を備えた注出管路54から注出して飲料水等に供する。
この第2実施例において、活性炭の再生を実施する場合
は、フロート型浄水槽60を水面から引き出して実施し
てもよい。また、図11では電極板79と端子棒76a
との接続関係を明らかにするため端子棒76aがフィル
タ74を貫通している状態を明示し、更に図12では電
極板79と端子棒76a及び絶縁部材78との位置関係
を明らかにするため、敢えて端子棒76a及び絶縁部材
78を図示した。
The purified water from which the dissolved substances have been removed from the raw water is then introduced into the second tank 80 after being filtered by the filters 81 and 82. The introduced purified water is irradiated with ultraviolet rays from a UV lamp 83, and ozone is also supplied from an ozone generator through an ozone introduction pipe 84. Thereby, bacteria of the purified water are sterilized, and algae, organic compounds, inorganic compounds, and the like are oxidatively decomposed. The treated water thus purified and sterilized is sucked into the self-contained pump 61 through the suction pipe 85, discharged from the tip of the discharge pipe 57, and returned into the water tank 50. Repeated circulation back to the purification and sterilization pumping raw water, when using purification sterilization water in the water tank 50 is pouring valve 53
And supplied to drinking water and the like from the discharge pipe 54 provided with.
In the case of regenerating activated carbon in the second embodiment
Is carried out by pulling out the float type water purifying tank 60 from the water surface.
You may. In FIG. 11, the electrode plate 79 and the terminal rod 76a are shown.
Terminal rod 76a fills up to clarify the connection relationship with
FIG. 12 clearly shows a state in which the
Positional relationship between electrode plate 79, terminal rod 76a and insulating member 78
In order to make the terminal rod 76a and the insulating member
78 is illustrated.

【0041】なお、本発明の第1、第2実施例では、活
性炭の再生時期の目安に自給式ポンプの吐出流量の累積
設定量を目標にして、この累積設定量を越えたか否かを
検出して再生制御を行う方法が採られた。しかし、本発
明では、電圧印加タイマに代えて活性炭(または槽本
体)の温度を検出する手段を設け、この検出温度が設定
温度を越えたか否かを検出して、電極に印加される電圧
をオンオフする制御も可能である。図14は、活性炭の
検出温度と電極印加電圧との相関を示す特性曲線であ
る。この場合の吸着物質の脱離効率ηは、活性炭の形態
が繊維状の場合の脱離効率をη、粒状の場合をη
すると、印加電圧1時間で繊維状の活性炭の方が脱離効
率が高いことが理解される。また、同図において、活性
炭をヒータ等で電気加熱した場合(曲線T)、かなり高
い効率で脱離が可能になることも示されている。
In the first and second embodiments of the present invention, the cumulative set amount of the discharge flow rate of the self-contained pump is set as a target for the regeneration timing of the activated carbon, and whether or not the cumulative set amount is exceeded. A method of detecting the presence or absence and performing reproduction control has been adopted. However, in the present invention, a means for detecting the temperature of the activated carbon (or the tank body) is provided in place of the voltage application timer, and it is detected whether or not the detected temperature exceeds a set temperature, and the voltage applied to the electrode is reduced. On / off control is also possible. FIG. 14 is a characteristic curve showing the correlation between the detected temperature of activated carbon and the voltage applied to the electrode. In this case, assuming that the desorption efficiency η of the adsorbed substance is η 1 when the form of the activated carbon is fibrous and η 2 when the form of the activated carbon is fibrous, the fibrous activated carbon desorbs in one hour at an applied voltage It is understood that the separation efficiency is high. Further, FIG. 3 also shows that when activated carbon is electrically heated by a heater or the like (curve T), desorption can be performed with considerably high efficiency.

【0042】[0042]

【発明の効果】以上説明したように、本発明による請求
項1、2の浄水装置は、原水供給源の供給水圧もしくは
ポンプを用いて吐出される浄化処理水の累積量が設定量
を越えたとき、これを流量検出手段によって検出して吸
着剤を再生する時期としているため、的確な再生によっ
て吸着剤はもとより装置の耐久性を高める効果がある。
As described above, according to the water purifying apparatus of the first and second aspects of the present invention, the supply water pressure of the raw water supply source or the accumulated amount of the purified water discharged using the pump exceeds the set amount. At this time, since the time is detected by the flow rate detecting means to regenerate the adsorbent, there is an effect of improving the durability of the device as well as the adsorbent by proper regeneration.

【0043】請求項3〜6の発明では、再生に先駆けて
残存の原水を外部排水し、再生時に電極間に電圧を印加
して吸着剤を加熱するため、吸着物質を効果的に脱離さ
せることができる。
According to the third to sixth aspects of the present invention, the remaining raw water is drained externally prior to regeneration, and a voltage is applied between the electrodes during regeneration to heat the adsorbent, so that the adsorbed substance is effectively desorbed. be able to.

【0044】請求項7の発明では、電圧印加による吸着
剤の加熱時に、吸着剤の温度が設定温度を越えた場合は
電極への電圧印加を停止できるので消費電力の節減の面
でも有効である。
According to the seventh aspect of the present invention, when the adsorbent is heated by applying a voltage, if the temperature of the adsorbent exceeds a set temperature, the application of the voltage to the electrodes can be stopped, which is effective in saving power consumption. .

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

【図1】本発明による浄水装置の第1実施例の断面図FIG. 1 is a sectional view of a first embodiment of a water purification device according to the present invention.

【図2】第1実施例の電極の平面図FIG. 2 is a plan view of the electrode of the first embodiment.

【図3】図2の電極の断面図FIG. 3 is a sectional view of the electrode of FIG. 2;

【図4】第1実施例の電極と取付板との平面図FIG. 4 is a plan view of an electrode and a mounting plate of the first embodiment.

【図5】図4の電極の断面図FIG. 5 is a sectional view of the electrode of FIG. 4;

【図6】実施例の制御回路のブロック図FIG. 6 is a block diagram of a control circuit according to the embodiment;

【図7】実施例の装置の動作態様を示すフローチャートFIG. 7 is a flowchart showing an operation mode of the apparatus according to the embodiment.

【図8】再生時の印加電圧との相関を示すタイムチャー
FIG. 8 is a time chart showing a correlation with an applied voltage during reproduction.

【図9】再生時の設定積算流量との相関を示すタイムチ
ャート
FIG. 9 is a time chart showing a correlation with a set integrated flow rate during regeneration.

【図10】本発明による浄水装置の第2実施例であるフ
ロート型の断面図
FIG. 10 is a sectional view of a float type water purification apparatus according to a second embodiment of the present invention.

【図11】第2実施例の電極部周辺の断面図FIG. 11 is a cross-sectional view around an electrode portion of the second embodiment.

【図12】図11の平面断面図FIG. 12 is a plan sectional view of FIG. 11;

【図13】第2実施例の変形例としての電極部周辺の断
面図
FIG. 13 is a sectional view around an electrode portion as a modification of the second embodiment.

【図14】吸着剤である活性炭の検出温度と電極印加電
圧との相関を示す特性曲線図
FIG. 14 is a characteristic curve diagram showing the correlation between the detected temperature of activated carbon as an adsorbent and the voltage applied to the electrode.

【符号の説明】[Explanation of symbols]

10…本体槽、11…原水導入口、12、35…三方向
電磁切換弁、20…フィルタ部材、21…外周側フィル
タ、22…内周側フィルタ、23…活性炭(吸着剤)、
25,26…電極、27…取付板、29…中央貯水部、
30…UVランプ、31…オゾン導入管、32…自給式
ポンプ、33…吸入管、34…吐出管、36…流量検出
器、40…制御装置、60…フロート型浄水装置。
DESCRIPTION OF SYMBOLS 10 ... Main body tank, 11 ... Raw water introduction port, 12, 35 ... Three-way electromagnetic switching valve, 20 ... Filter member, 21 ... Outer periphery filter, 22 ... Inner periphery filter, 23 ... Activated carbon (adsorbent),
25, 26 ... electrode, 27 ... mounting plate, 29 ... central water storage,
30 UV lamp, 31 ozone introduction pipe, 32 self-contained pump, 33 suction pipe, 34 discharge pipe, 36 flow rate detector, 40 control device, 60 float type water purification device.

Claims (7)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 電圧を印加すると自己発熱する吸着剤に
原水を接触させる槽と、 吸着剤に接触または埋没して電圧を印加する一対の電極
と、 吸着剤との接触により浄化された処理水の累積量が設定
量を越えたことを検出する流量検出手段と、 流量検出手段から検出信号が出力されたとき電極間に電
圧を印加する制御信号を送出する制御装置とを備えたこ
とを特徴とする浄水装置。
1. A tank for bringing raw water into contact with an adsorbent that generates heat when a voltage is applied, a pair of electrodes that contact or bury the adsorbent to apply a voltage, and treated water purified by contact with the adsorbent. features of the flow rate detecting means for detecting that the accumulated amount exceeds a set amount, further comprising a controller for sending a control signal for applying a voltage between the electrodes when a detection signal from the flow rate detecting means is outputted And water purification equipment.
【請求項2】 処理水を吸引して吐出するポンプを設
け、 ポンプから吐出される処理水の累積量が設定量を越えた
ことを流量検出手段によって検出し、検出信号に基づい
て制御装置からポンプの運転を停止させるオフ信号を送
出すると共に、電極間に電圧を印加する制御信号を送出
する請求項1記載の浄水装置。
2. A pump for sucking and discharging treated water is provided, a flow rate detecting means detects that a cumulative amount of treated water discharged from the pump exceeds a set amount, and a control device based on the detected signal. The water purification device according to claim 1, wherein an off signal for stopping operation of the pump is sent, and a control signal for applying a voltage between the electrodes is sent.
【請求項3】 原水の通過可能な外周側フィルタ及び内
周側フィルタからなる二重筒体中に吸着剤を収容したフ
ィルタ部材を槽の内部に軸線を垂直方向に合わせて配置
し、内周側フィルタの内側空間の貯水部に処理水を収容
する請求項1記載の浄水装置。
3. A filter member containing an adsorbent in a double cylindrical body composed of an outer filter and an inner filter through which raw water can pass, is disposed inside the tank so that the axis is aligned in the vertical direction. The water purification device according to claim 1, wherein the treated water is stored in a water storage part in an inner space of the side filter.
【請求項4】 電極が、二重筒体のフィルタ部材の上下
開口部を閉塞する輪環状に成形されて吸着剤に接触可能
である請求項1記載の浄水装置。
4. The water purification apparatus according to claim 1, wherein the electrode is formed in an annular shape for closing the upper and lower openings of the double cylindrical filter member and is capable of contacting the adsorbent.
【請求項5】 再生信号の送出前に貯水部を含む槽内全
域から原水を排水して抜き取る請求項1記載の浄水装
置。
5. The water purification apparatus according to claim 1, wherein the raw water is drained and extracted from the entire area including the water storage section before sending the reproduction signal.
【請求項6】 槽内に原水を導入する導入管に切換弁を
設け、制御装置からの切換信号による切換弁の切り替え
で貯水部を含む槽内全域から原水を排水して抜き取る請
求項1又は請求項4記載の浄水装置。
6. The switching valve to the introduction pipe for introducing the raw water provided in the tank is withdrawn and drained raw water from the bath in the entire region including the water storage section with the switching of the switching valve according to the switching signal from the control device according to claim 1 or The water purification device according to claim 4.
【請求項7】 吸着剤中に温度検出手段を配し、吸着剤
の温度が設定温度を越えたことの検出信号に基づいて電
極にオフ信号を送出して電圧印加を停止する請求項1記
載の浄水装置。
7. The method according to claim 1, further comprising the step of: disposing a temperature detecting means in the adsorbent, sending an off signal to the electrode based on a detection signal indicating that the temperature of the adsorbent has exceeded a set temperature, and stopping the voltage application. Water purification equipment.
JP3054293A 1993-02-19 1993-02-19 Water purification equipment Expired - Fee Related JP2744395B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3054293A JP2744395B2 (en) 1993-02-19 1993-02-19 Water purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3054293A JP2744395B2 (en) 1993-02-19 1993-02-19 Water purification equipment

Publications (2)

Publication Number Publication Date
JPH06238264A JPH06238264A (en) 1994-08-30
JP2744395B2 true JP2744395B2 (en) 1998-04-28

Family

ID=12306687

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3054293A Expired - Fee Related JP2744395B2 (en) 1993-02-19 1993-02-19 Water purification equipment

Country Status (1)

Country Link
JP (1) JP2744395B2 (en)

Also Published As

Publication number Publication date
JPH06238264A (en) 1994-08-30

Similar Documents

Publication Publication Date Title
JP2004505770A (en) Water treatment system under the sink
JP2002059152A (en) System for cleaning water
JPH1028973A (en) Water purifying device
CN104098218B (en) Water-purifying process and water purifying plant thereof
JP2744395B2 (en) Water purification equipment
JPH06182330A (en) Water purification device
JPH0639372A (en) Water purifying system
KR101313679B1 (en) Device for activating liquids
JP3080808B2 (en) Water purification device and method of using the same
JP2002355672A (en) Method and device for water treatment
JP3215720B2 (en) Water purification equipment
JPH0639373A (en) Water purifying system
JP3742454B2 (en) Clean water supply device
JP3841926B2 (en) Water purification device
JP3069019U (en) Activated ordinary water production equipment
JPH10470A (en) Wastewater treatment apparatus
JPH10235361A (en) Water purifier for porous carbon electrode regenerating type and regeneration of the same
JPH0731970A (en) Method for regenerating adsorbent of water purifying and sterilizing device
JPH06182331A (en) Float type water purification device
KR200157785Y1 (en) Domestic water purifying plant
JPH06246260A (en) Water purifying device
JP2536392B2 (en) Purification unit
RU2103230C1 (en) Water supply plant
JPH0724445A (en) Water purifying and sterilizing device
JPH10328650A (en) Apparatus for purifying and disinfecting water

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees