JP3239304B2 - Water purification equipment - Google Patents
Water purification equipmentInfo
- Publication number
- JP3239304B2 JP3239304B2 JP27454292A JP27454292A JP3239304B2 JP 3239304 B2 JP3239304 B2 JP 3239304B2 JP 27454292 A JP27454292 A JP 27454292A JP 27454292 A JP27454292 A JP 27454292A JP 3239304 B2 JP3239304 B2 JP 3239304B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- water purification
- purification tank
- tank
- pressure
- 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
Links
Landscapes
- Water Treatment By Sorption (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、一般家庭用及び業務用
飲料水の浄水装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for purifying drinking water for domestic and commercial use.
【0002】[0002]
【従来の技術】近年、水道水をそのまま飲料水として使
用するよりも、活性炭等を利用して浄化するようにした
浄水器が広く一般に普及している。2. Description of the Related Art In recent years, water purifiers that purify water using activated carbon or the like rather than using tap water as drinking water as they are are widely and widely used.
【0003】[0003]
【発明が解決しようとする課題】ところで、このような
従来から使用されてきた浄水器の場合、使用年数が高ま
って活性炭に有機塩素系化合物等の物質が物理的に吸着
されると、活性化機能が低下する。この機能低下した活
性炭を活性化させて再生するには、吸着物質の脱離が行
われる。However, in the case of such a conventionally used water purifier, when the life of the water purifier is increased and a substance such as an organic chlorine compound is physically adsorbed on the activated carbon, the activated water purifier is activated. Function deteriorates. In order to activate and regenerate the activated carbon whose function has been reduced, the adsorbed substance is desorbed.
【0004】吸着物質の脱離には、浄水槽に温水や加熱
蒸気を通す方法が知られている。こうした脱離方法では
吸着物質の約70%程度の脱離が可能であるが、長時間
を要し効率面で問題があった。[0004] A known method for removing adsorbed substances is to pass hot water or heated steam through a water purification tank. With such a desorption method, about 70% of the adsorbed substance can be desorbed, but it takes a long time and there is a problem in efficiency.
【0005】従って、本発明は、吸着物質を効率的に短
時間で脱離させて再生可能にした浄水装置を提供するこ
とを目的としている。[0005] Accordingly, an object of the present invention is to provide a water purification apparatus capable of regenerating an adsorbed substance by efficiently desorbing the adsorbed substance in a short time.
【0006】[0006]
【課題を解決するための手段】本発明は前記課題を解決
するため、請求項1の発明は、浄水槽内に充填された活
性炭に吸着した物質を脱離させて再生するとき、排水に
よって浄水槽内を減圧する減圧手段と浄水槽内に加熱蒸
気を送る蒸気供給手段とを備え、浄水槽内の減圧と浄水
槽内への加熱蒸気供給を同時に行いまたは交互に数回繰
り返す構成となっている。これにより、活性炭に吸着し
た物質を確実かつ効率的に脱離することができる。 ま
た、請求項2の発明は、請求項1の浄水装置において、
減圧手段が、原水の供給が停止された状態で浄水槽内の
排水を行う排水管路と、排水時に排水管路を開く排水弁
と、排水管路の排水流圧を受け手浄水槽内を吸引して減
圧するアスピレータとを備えた構成となっている。この
アスピレータによって、原水の供給が停止された状態で
排水管路から浄水槽内の排水を行い、排水流圧を受けて
浄水槽内を吸引して減圧する。 更に、請求項3の発明
は、請求項1又は請求項2の浄水装置において、活性炭
に吸着した物質を紫外線で分解する紫外線ランプを浄水
槽内に配置した構成となっている。これにより、活性炭
の吸着物質が分解され、吸着物質の脱離が一層効果的に
行われる。 The present invention solves the above-mentioned problems.
In order to achieve this, the invention of claim 1 relies on the activity filled in the water purification tank.
When desorbing and regenerating substances adsorbed on charcoal,
Therefore, decompression means for depressurizing the inside of the water purification tank and heating steam
Equipped with a steam supply means for sending air, reducing the pressure inside the water purification tank and purifying the water.
Supply heating steam into the tank simultaneously or alternately several times.
It is configured to return. As a result, it is adsorbed on activated carbon
Can be reliably and efficiently desorbed. Ma
The invention according to claim 2 is the water purification device according to claim 1,
The decompression means is used to stop the supply of raw water and
Drainage pipe for drainage and drainage valve that opens drainage pipe when draining
The suction pressure in the water treatment tank is reduced by the
And a pressurizing aspirator. this
With the supply of raw water stopped by the aspirator
Drains the water in the water purifier from the drain pipe and receives the drain pressure.
The pressure inside the water purification tank is reduced by suction. Further, the invention of claim 3
Is the activated carbon in the water purifier according to claim 1 or 2.
Purifies UV lamps that decompose substances adsorbed on the surface with UV light
It is configured to be placed inside the tank. With this, activated carbon
Of the adsorbed material is decomposed, and the desorption of the adsorbed material is more effective
Done.
【0007】[0007]
【0008】[0008]
【0009】[0009]
【0010】[0010]
【0011】[0011]
【0012】[0012]
【0013】[0013]
【0014】[0014]
【0015】[0015]
【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に示すように、実施例の浄水装置10
は、原水である水道水を供給して浄化後に給水栓から使
用に際し注出するに至るまでのメイン管路11を有し、
このメイン管路11には浄水槽14が設けられている。
またメイン管路11には殺菌槽等も設けられることもあ
るがここではそれらの説明は省略する。浄水槽14には
活性炭16が前後のフィルタ15を介して充填され、原
水を活性炭16に通して浄化するようになっている。As shown in FIG. 1, a water purification apparatus 10 according to an embodiment
Has a main pipe line 11 that supplies tap water, which is raw water, from the hydrant to the outlet after use for purification.
A water purification tank 14 is provided in the main conduit 11.
In addition, a sterilization tank or the like may be provided in the main conduit 11, but the description thereof is omitted here. Activated carbon 16 is filled in the water purification tank 14 via the front and rear filters 15, and the raw water is passed through the activated carbon 16 to purify the water.
【0018】浄水槽14の上流入口側でメイン管路11
には、浄水槽14への給水を制限する電磁式の給水弁1
2が設けられ、閉弁により浄水槽20に原水の供給を停
止できる。浄水槽20の下流出口側でメイン管路11に
は注水弁13が設けられ、この注水弁13を開き操作し
て使用に供することができる。At the upstream inlet side of the water purification tank 14, the main pipeline 11
Has an electromagnetic water supply valve 1 that restricts water supply to the water purification tank 14.
2 is provided, and the supply of raw water to the water purification tank 20 can be stopped by closing the valve. A water injection valve 13 is provided in the main pipeline 11 at the downstream outlet side of the water purification tank 20, and the water injection valve 13 can be opened and used for use.
【0019】また、浄水槽14からは、実施例では図示
のように入口側に排水管路20が設けられ、この排水管
路20には上流側の浄水槽14から順に逆止弁21、本
発明でいう減圧手段のアスピレータ22、そして電磁弁
による排水弁23が配置されている。アスピレータ22
は、周知のように水流によって空気その他の気体を吸引
する器具であり、実施例では浄水槽14からの排水時、
排水弁23の開弁によって排水管路20に発生する水流
圧を受けて作動し、浄水槽14の内部を吸引して減圧す
るようになっている。In the embodiment, a drain pipe 20 is provided on the inlet side of the water purification tank 14 as shown in the figure. An aspirator 22, which is a pressure reducing means referred to in the present invention, and a drain valve 23, which is an electromagnetic valve, are provided. Aspirator 22
Is a device for sucking air or other gas by a water flow as is well known, and in the embodiment, when draining from the water purification tank 14,
When the drain valve 23 is opened, it operates by receiving a water flow pressure generated in the drain pipe 20, and sucks the inside of the water purification tank 14 to reduce the pressure.
【0020】また、メイン管路11においては、浄水槽
14を迂回して給水弁12の上流側とアスピレータ22
がバイパス管路30によって接続されている。従って、
アスピレータ22にはバイパス管路30から直接原水が
導入可能である。アスピレータ22に原水を導入する意
味は、この原水によって浄水槽14からの排水時に伴っ
て排水管路20に発生する水流を引っ張るためであり、
効果的に水流圧を発生させるためである。In the main pipe 11, the water is bypassed from the water purification tank 14 to the upstream of the water supply valve 12 and the aspirator 22.
Are connected by a bypass line 30. Therefore,
Raw water can be directly introduced into the aspirator 22 from the bypass line 30. The reason for introducing the raw water into the aspirator 22 is that the raw water pulls the water flow generated in the drainage pipe 20 due to the drainage from the water purification tank 14,
This is for effectively generating the water pressure.
【0021】一方、バイパス管路30と浄水槽14の下
流側は、蒸気供給手段を構成する蒸気供給管路40で接
続され、この蒸気供給管路40には同じく蒸気供給手段
を構成するヒータ装置41が設けられている。ヒータ装
置41は加熱槽42を有し、ここにはバイパス管路30
から原水導入管路47を通して原水が導入されるように
なっている。加熱槽42の外周囲にはヒータ43が巻き
付けてあり、ヒータ43への通電によって加熱槽42内
の原水を加熱して蒸発させることが可能である。加熱槽
42内の原水の水位はセンサ44で検出するようになっ
ていて、原水の所定の水位を保持して加熱槽42の空焚
き防止を可能にしている。加熱槽42の上流側で原水導
入管路47には電磁弁による第1開閉弁45が設けら
れ、水位センサ44の検出信号に基づいた制御装置50
からの動作信号でもって第1開閉弁45の開閉を制御
し、加熱槽42に導入する原水量の調整が行われる。加
熱槽42と浄水槽14との間には第2開閉弁46が設け
られ、加熱槽42から浄水槽14に送られる加熱蒸気の
導入を制限する。On the other hand, the bypass line 30 and the downstream side of the water purification tank 14 are connected by a steam supply line 40 constituting steam supply means, and the steam supply line 40 has a heater device which also constitutes steam supply means. 41 are provided. The heater device 41 has a heating tank 42 in which the bypass line 30 is provided.
The raw water is introduced through a raw water introduction pipe 47 from the outlet. A heater 43 is wound around the outer periphery of the heating tank 42, and it is possible to heat and evaporate the raw water in the heating tank 42 by energizing the heater 43. The level of the raw water in the heating tank 42 is detected by a sensor 44, and a predetermined water level of the raw water is maintained to prevent the heating tank 42 from being idle. A first opening / closing valve 45 provided by an electromagnetic valve is provided in the raw water introduction pipe 47 on the upstream side of the heating tank 42, and a control device 50 based on the detection signal of the water level sensor 44
The opening / closing of the first opening / closing valve 45 is controlled by the operation signal from the controller, and the amount of raw water introduced into the heating tank 42 is adjusted. A second opening / closing valve 46 is provided between the heating tank 42 and the water purification tank 14 to limit the introduction of the heating steam sent from the heating tank 42 to the water purification tank 14.
【0022】制御装置50は、図2の制御回路のブロッ
ク図に示すように、マイクロコンピュータ等により構成
されるCPU(中央演算装置)51、タイマー回路52
等からなっていて、I/Oポート53から外部機器の電
磁弁式給水弁12、排水弁23に動作信号を送出して各
弁の開閉を制御するとともに、水位センサ44からの検
出信号を受けて第1、第2開閉弁45、46に動作信号
を送って開閉制御し、またヒータ43への通電をオンオ
フさせる制御信号を送出するなどの各種制御が可能であ
る。またタイマー回路52によって、浄水槽14内の減
圧と加熱蒸気供給の2つの行程を好適なインターバルで
交互に、後述するように数回繰り返すことできる。As shown in the block diagram of the control circuit in FIG. 2, the control device 50 includes a CPU (central processing unit) 51 composed of a microcomputer and the like, and a timer circuit 52.
An operation signal is transmitted from the I / O port 53 to the electromagnetic valve type water supply valve 12 and the drain valve 23 of the external device to control the opening and closing of each valve, and receives a detection signal from the water level sensor 44. Various controls are possible such as sending an operation signal to the first and second opening / closing valves 45 and 46 to perform opening / closing control, and sending a control signal for turning on / off the power supply to the heater 43. Further, the timer circuit 52 can alternately repeat the two processes of reducing the pressure in the water purification tank 14 and supplying the heated steam several times at suitable intervals, as described later.
【0023】次に、以上の構成による実施例の浄水装置
の作用を図3の動作フローチャートと図4のタイムチャ
ートを併用して説明する。Next, the operation of the water purification apparatus according to the embodiment having the above configuration will be described with reference to the operation flowchart of FIG. 3 and the time chart of FIG.
【0024】通常使用時、原水の水道水はメイン管路1
1から浄水槽14に送られ、活性炭16に接触して浄化
される。浄化水は好適な飲料水等として注水弁13の操
作により使用に供される。During normal use, the tap water of the raw water is supplied to the main line 1
From 1 the water is sent to a water purification tank 14 where it contacts the activated carbon 16 and is purified. The purified water is used by operating the water injection valve 13 as a suitable drinking water or the like.
【0025】長期使用によって、浄水槽14の活性炭1
6に有機塩素系化合物等による物質が物理的に吸着する
と、それ以上使用に好ましくないとの判断がなされる。
吸着物質の検出には種々の方法が考えられ、吸着量が定
量以下か以上かは基準値との比較を例えばコンピュータ
制御で自動検出して判断する方法などが採用される。こ
こでは判断の方法について特に限定しない。制御装置5
0から例えば警報ランプの点滅方法などで活性炭16の
再生指示が報知され、次の段階で制御装置50では再生
制御を開始する(ステップS1)。The long-term use of the activated carbon 1 in the water purification tank 14
If a substance such as an organic chlorine-based compound is physically adsorbed on 6, it is determined that it is not preferable for further use.
Various methods are conceivable for detecting the adsorbed substance. For example, a method of automatically detecting and comparing with a reference value by a computer control to determine whether the amount of adsorption is equal to or less than a fixed amount is adopted. Here, the method of determination is not particularly limited. Control device 5
From 0, an instruction to regenerate the activated carbon 16 is notified by, for example, a blinking method of an alarm lamp, and the control device 50 starts regeneration control in the next stage (step S1).
【0026】まず、制御装置50からメイン管路11の
上流側給水弁12にオフ信号が送られ、給水弁12が閉
じてそれまで浄水槽14への原水供給を停止する(ステ
ップS2)。これにほぼ同期して、オン信号が排水弁2
3に送られ、排水弁23が開いて排水管路20から浄水
槽14内の排水が開始される(ステップS3)。浄水槽
14では原水供給が停止されているので、排水が進むと
ともに内部が次第に負圧化する。このとき、アスピレー
タ22には浄水槽14を迂回した原水がバイパス管路3
0から導入され、排水管路20の排水に伴ってアスピレ
ータ22が動作し、浄水槽14の内部を吸引して減圧す
る。浄水槽14では、減圧によって活性炭16に吸着し
た物質が次第に脱離する。First, an OFF signal is sent from the control device 50 to the upstream water supply valve 12 of the main pipeline 11, the water supply valve 12 is closed, and the supply of raw water to the water purification tank 14 is stopped until then (step S2). Almost in synchronization with this, the ON signal is output to the drain valve 2
3 and the drain valve 23 is opened to start draining the water from the drain pipe 20 into the water purification tank 14 (step S3). Since the supply of raw water is stopped in the water purification tank 14, as the drainage proceeds, the pressure inside the water gradually decreases. At this time, the raw water bypassing the water purification tank 14 is supplied to the aspirator 22 by the bypass pipe 3.
The aspirator 22 is operated in accordance with the drainage of the drainage pipe 20, and the inside of the water purification tank 14 is sucked to reduce the pressure. In the water purification tank 14, the substances adsorbed on the activated carbon 16 due to the reduced pressure gradually desorb.
【0027】図4のように、アスピレータ22による減
圧はタイマー回路52によって所定時間T1行われ(ス
テップS4)、次行程の加熱蒸気供給(時間T2)の行
程と交互に所定のインターバルで繰り返し行われ、制御
装置50ではCPU51にその繰り返し数Nが設定して
ある。As shown in FIG. 4, the pressure reduction by the aspirator 22 is performed by the timer circuit 52 for a predetermined time T 1 (step S 4), and is repeated at predetermined intervals alternately with the next heating steam supply (time T 2 ). The repetition number N is set in the control device 50 in the CPU 51.
【0028】一方、浄水槽14内の減圧が行われている
間、活性炭16では物質の脱離が進行する。例えば、減
圧開始と同時に、制御装置50から第1開閉弁45にオ
ン信号が送られ、第1開閉弁45が開いて浄水槽14を
迂回した原水がバイパス管路30から原水導入管路47
に流れ込み、ヒーター装置41の加熱槽42内に導入さ
れる。このヒータ装置41では、加熱槽42に所定量の
原水が導入されたタイミングを計ってヒータ43に通電
の信号が送られ、加熱槽42内の原水を加熱して蒸発さ
せる。On the other hand, while the pressure in the water purification tank 14 is being reduced, the desorption of the substance proceeds in the activated carbon 16. For example, at the same time as the start of the depressurization, an ON signal is sent from the control device 50 to the first on-off valve 45, the first on-off valve 45 is opened, and the raw water that has bypassed the water purification tank 14 flows from the bypass line 30 into the raw water introduction line 47.
And is introduced into the heating tank 42 of the heater device 41. In the heater device 41, an energization signal is sent to the heater 43 at a timing when a predetermined amount of raw water is introduced into the heating tank 42, and the raw water in the heating tank 42 is heated and evaporated.
【0029】減圧時間T1がタイムアップすると、制御
装置50から蒸気供給管路40の第2開閉弁46にオン
信号が送られ、この第2開閉弁46が開いてヒータ装置
41から加熱蒸気が浄水槽14内に導入される(ステッ
プS5)。減圧下の浄水槽14内に加熱蒸気の導入によ
って、活性炭16に吸着した物質の減圧による脱離が更
に促進される。即ち、減圧時間T1に続いて蒸気供給を
時間T2だけ交互に設定回数N回まで繰り返す(ステッ
プS5)。これによって、吸着物質の脱離が短時間で再
生効果を一層高めることができる。When the depressurization time T 1 has elapsed, an ON signal is sent from the control device 50 to the second opening / closing valve 46 of the steam supply line 40, and the second opening / closing valve 46 is opened, and the heated steam is supplied from the heater device 41. It is introduced into the water purification tank 14 (step S5). By introducing heated steam into the water purification tank 14 under reduced pressure, desorption of the substance adsorbed on the activated carbon 16 by reduced pressure is further promoted. In other words, following the decompression time T 1 repeats the steam supply to the set number of times N times alternately by time T 2 (step S5). Thereby, desorption of the adsorbed substance can further enhance the regenerating effect in a short time.
【0030】加熱槽42で原水の加熱中、原水がなくな
った状態での空焚きが防止される。即ち、加熱槽42へ
の導入原水量を常時一定に保持するため、水位センサ4
4は所定の原水レベルを検出して信号を制御装置50に
送り、制御装置50からの動作信号で原水導入管路47
の第1開閉弁45の開閉を管理し、バイパス管路30か
ら加熱槽42への原水供給に過不足がないように制御を
行う。During the heating of the raw water in the heating tank 42, the empty firing in a state where the raw water is exhausted is prevented. That is, in order to always keep the amount of raw water introduced into the heating tank 42 constant, the water level sensor 4
4 detects a predetermined raw water level, sends a signal to the control device 50, and receives an operation signal from the control device 50 to supply a raw water introduction line 47.
The opening and closing of the first on-off valve 45 is controlled, and control is performed such that the supply of raw water from the bypass pipe 30 to the heating tank 42 is not excessive or insufficient.
【0031】なお、本発明の浄水装置10では、他の実
施例として、電磁式の第1開閉弁45に代えて三方向切
換弁とすることもできる。また、浄水槽14の内部に紫
外線ランプ(図示せず)を配置し、前述のように減圧と
蒸気供給の2つの行程を数回繰り返す間に、これらに併
行して紫外線を活性炭16に照射し、吸着した物質の分
解を行い、脱離を促進させて活性炭16の再生効率を更
に高めることが可能である。In the water purifier 10 of the present invention, as another embodiment, a three-way switching valve may be used instead of the electromagnetic first opening / closing valve 45. Further, an ultraviolet lamp (not shown) is disposed inside the water purification tank 14, and while the two steps of depressurization and steam supply are repeated several times as described above, the activated carbon 16 is irradiated with ultraviolet light concurrently therewith. In addition, it is possible to decompose the adsorbed substance and promote the desorption thereof to further increase the regeneration efficiency of the activated carbon 16.
【0032】[0032]
【発明の効果】以上説明したように、請求項1及び請求
項2の発明によれば、浄水槽の活性炭に吸着した物質を
脱離させて再生する際、浄水槽内の減圧と浄水槽内への
加熱蒸気供給を同時に行いまたは交互に数回繰り返す構
成となっているので、活性炭に吸着した物質を確実かつ
効率的に脱離することができる。請求項3の発明によれ
ば、請求項1の発明及び請求項2の発明の効果に加え
て、紫外線より活性炭の吸着物質が分解され、吸着物質
の脱離が一層効果的に行われるという効果を有する。 As described above, claims 1 and 2
According to the invention of Item 2, when the substance adsorbed on the activated carbon in the water purification tank is desorbed and regenerated , the pressure in the water purification tank and the pressure in the water purification tank are reduced.
A configuration in which heating steam is supplied simultaneously or alternately several times
The material adsorbed on the activated carbon
It can be efficiently desorbed. According to the invention of claim 3
In addition to the effects of the invention of claim 1 and the invention of claim 2,
The activated carbon is decomposed by ultraviolet light,
Is more effectively eliminated.
【0033】[0033]
【0034】[0034]
【0035】[0035]
【図1】本発明による浄水装置の実施例の構成図FIG. 1 is a configuration diagram of an embodiment of a water purification device according to the present invention.
【図2】実施例の浄水装置における制御装置のブロック
図FIG. 2 is a block diagram of a control device in the water purification apparatus of the embodiment.
【図3】実施例の浄水装置の動作フローチャートFIG. 3 is an operation flowchart of the water purification apparatus of the embodiment.
【図4】実施例の浄水装置における減圧と加熱蒸気供給
のタイムチャートFIG. 4 is a time chart of pressure reduction and supply of heated steam in the water purification apparatus of the embodiment.
10…浄水槽、11…メイン管路、12、23、45、
46…電磁式開閉弁、14…浄水槽、16…活性炭、2
0…排水管路、22…アスピレータ(減圧手段)、30
…バイパス管路、40…蒸気供給管路、41…ヒータ装
置、42…加熱槽、43…ヒータ、44…水位センサ、
45、46…第1、第2開閉弁、47…原水導入管路。10: water purification tank, 11: main pipeline, 12, 23, 45,
46: solenoid on-off valve, 14: water purification tank, 16: activated carbon, 2
0: drainage pipe, 22: aspirator (decompression means), 30
... bypass line, 40 ... steam supply line, 41 ... heater device, 42 ... heating tank, 43 ... heater, 44 ... water level sensor,
45, 46: First and second on-off valves, 47: Raw water introduction pipeline.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 1/28 C02F 1/44 B01D 35/04 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) C02F 1/28 C02F 1/44 B01D 35/04
Claims (3)
物質を脱離させて再生するとき、排水によって浄水槽内
を減圧する減圧手段と浄水槽内に加熱蒸気を送る蒸気供
給手段とを備え、浄水槽内の減圧と浄水槽内への加熱蒸
気供給を同時に行いまたは交互に数回繰り返すことを特
徴とする浄水装置。When a substance adsorbed on activated carbon filled in a water purification tank is desorbed and regenerated, decompression means for reducing the pressure in the water purification tank by drainage and a steam supply for feeding heated steam into the water purification tank are provided.
Supply means , decompression inside the water purification tank and heating and steaming inside the water purification tank.
A water purification apparatus characterized in that air supply is performed simultaneously or alternately several times .
た状態で浄水槽内の排水を行う排水管路と、排水時に排
水管路を開く排水弁と、排水管路の排水流圧を受けて浄
水槽内を吸引して減圧するアスピレータとを備えたこと
を特徴とする請求項1記載の浄水装置。2. The pressure reducing means stops supply of raw water.
Drainage line for draining water from the water purification tank
A drain valve that opens the water pipe and the drainage pressure of the drain pipe
The water purifier according to claim 1, further comprising: an aspirator that suctions the inside of the water tank to reduce the pressure .
る紫外線ランプを浄水槽内に配置したことを特徴とする
請求項1又は請求項2記載の浄水装置。3. The substance adsorbed on the activated carbon is decomposed by ultraviolet rays.
The water purifier according to claim 1 or 2, wherein an ultraviolet lamp is disposed in the water purifier.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27454292A JP3239304B2 (en) | 1992-10-13 | 1992-10-13 | Water purification equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27454292A JP3239304B2 (en) | 1992-10-13 | 1992-10-13 | Water purification equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06126272A JPH06126272A (en) | 1994-05-10 |
| JP3239304B2 true JP3239304B2 (en) | 2001-12-17 |
Family
ID=17543169
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27454292A Expired - Fee Related JP3239304B2 (en) | 1992-10-13 | 1992-10-13 | Water purification equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3239304B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101158898B1 (en) * | 2012-02-22 | 2012-06-25 | (주)윈텍글로비스 | Water treatment apparatus and water treatment method |
-
1992
- 1992-10-13 JP JP27454292A patent/JP3239304B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06126272A (en) | 1994-05-10 |
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