JP2004000989A - Water purification apparatus - Google Patents

Water purification apparatus Download PDF

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JP2004000989A
JP2004000989A JP2003286852A JP2003286852A JP2004000989A JP 2004000989 A JP2004000989 A JP 2004000989A JP 2003286852 A JP2003286852 A JP 2003286852A JP 2003286852 A JP2003286852 A JP 2003286852A JP 2004000989 A JP2004000989 A JP 2004000989A
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silver
water
water purification
liter
purification device
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Masumi Tsutsumi
堤 増美
Izumi Komatsu
小松 泉
Takayuki Ando
安東 貴行
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YASUKAWA CONTROL KK
Yaskawa Electric Corp
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YASUKAWA CONTROL KK
Yaskawa Electric Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a water purification apparatus which enables safe and effective bacteriostasis for stagnant water in downstream piping of the water purification apparatus without adding chlorine. <P>SOLUTION: In the water purification apparatus, a silver addition device which adds silver of ≥10μg/l to the downstream piping of the apparatus is attached or a mechanism which adds silver of ≥10μg/l from the water purification apparatus to the downstream piping of the apparatus is disposed. <P>COPYRIGHT: (C)2004,JPO

Description

 本発明は、一般家庭や飲食店、清涼飲料水工場などに使用される浄水装置のうち、塩素を除去する機能を持ち、例えば、配管の途中に切り込んで設置する浄水装置に関する。 (4) The present invention relates to a water purification device having a function of removing chlorine, for example, a water purification device that is cut in the middle of piping and installed, among water purification devices used in general households, restaurants, soft drink factories, and the like.

 近年、水道水の汚染の進行により、異味異臭のもとになる塩素臭やかび臭の除去、あるいは発ガン性のあるトリハロメタンの除去のために浄水器が多用されるようになっている。一般家庭を例に取ると、蛇口直結型やトップシンク型、あるいはアンダーシンク型など蛇口に近い位置で浄水装置が使用されているが、使用者の多くからは瞬間通水量が少ないこと、フィルターの寿命が極めて短いことなどなどがこれら浄水装置に関する不満として挙げられている。そこでこれらの使用者の不満を解決するために、浄水装置を大型化し、瞬間の通水量や総濾過流量を大きくした浄水装置が考えられる。これらの浄水装置は配管途中に切り込んで使用する浄水装置となる(例えば、特許文献1参照)。
特開平9−122636号公報(第1図)
In recent years, due to the progress of tap water pollution, water purifiers have been frequently used for removing chlorine odor and musty odor which cause unpleasant odor, or for removing trihalomethane which has carcinogenic properties. In general households, for example, water purifiers are used close to the faucet, such as a faucet direct connection type, a top sink type, or an undersink type. The extremely short service life is cited as dissatisfaction with these water purification devices. Therefore, in order to solve these users' dissatisfaction, a water purification apparatus in which the size of the water purification apparatus is increased and the instantaneous water flow rate and the total filtration flow rate are increased is considered. These water purifiers become water purifiers that are used by being cut in the middle of piping (for example, see Patent Document 1).
JP-A-9-122636 (FIG. 1)

 ところが、従来の浄水装置の多くは水道水中に殺菌浄化を目的として注入されている塩素を除去するので、浄水装置を通過した後の水は塩素を取り除かれて殺菌性能が無くなる。蛇口までの配管が極めて短い蛇口直結型、トップシンク型、アンダーシンク型などの浄水装置では、塩素除去後の配管中の滞留水は毎朝の放流時間を定めるなどし、この水を捨てて使用することで配管の滞留水中で増加する細菌の処置を行ってきた。ところが、例えば屋外に設置する浄水装置では、浄水装置の設置場所から蛇口までが数メートル以上離れることもあり、この配管中の滞留水を例えば毎朝使用者が放流する様に取扱説明書等で規定しても、使用者が必ずしも十分な放流を行うとは限らない。そこで、何らかの方法で浄水装置の下流側配管の滞留水に対して制菌機能もしくは殺菌機能を持たせる必要が生じるが、ビルなどに設置されている上質水供給システムでは浄水装置通過後の浄水に対して人間が感じにくい濃度の塩素を添加することで、これらの制菌性能を維持してきた。しかしながら、塩素を添加するこの方法では、一度塩素を除去して浄化した水が塩素臭で味覚を低下させる問題があり、また、塩素の含まれた水を加熱して飲用する場合には、水中に含まれる有機物と塩素が高温領域で反応し、発ガン性のあるトリハロメタンを多く生成する可能性があるので、危険な水に戻る可能性がある。 However, most conventional water purifiers remove chlorine injected into tap water for the purpose of sterilization and purification, so that water after passing through the water purifier removes chlorine and loses sterilization performance. In water purifiers such as faucet direct connection type, top sink type and under sink type where the piping to the faucet is extremely short, the remaining water in the piping after chlorine removal is determined by setting the discharge time every morning, and this water is discarded and used As a result, the bacteria that increase in the residence water in the piping have been treated. However, for example, in the case of a water purifier installed outdoors, the distance from the installation location of the water purifier to the faucet may be several meters or more, and the user is required to discharge the accumulated water in the piping, for example, every morning by the user's manual. However, the user does not always perform sufficient release. Therefore, it is necessary to provide a bacteriostatic function or a sterilizing function to the stagnant water in the downstream piping of the water purification device by some method.However, in the high-quality water supply system installed in buildings, etc., the purified water after passing through the water purification device is required. On the other hand, these bacteriostatic properties have been maintained by adding chlorine at a concentration that is hardly felt by humans. However, in this method of adding chlorine, there is a problem that water purified by removing chlorine once reduces taste due to chlorine odor. The organic matter and chlorine contained in the water may react in a high temperature range, producing a large amount of carcinogenic trihalomethane, which may return to dangerous water.

 そこで本発明は、浄水装置において、味覚の低下を招いたり昇温により発ガン性物質を生成する危険性のある塩素を添加することなく、浄水装置の下流側配管の滞留水に対して安全で効果的な制菌方法を提供することを目的とするものである。 Therefore, the present invention provides a water purification device that is safe against accumulated water in the downstream piping of the water purification device without adding chlorine, which may cause a decrease in taste or generate a carcinogenic substance due to a rise in temperature. It is intended to provide an effective bacteriostatic method.

 上記課題を解決するため、本発明は、浄水装置の下流側配管に銀を10μg/リットル以上添加する銀添加装置を付加した浄水装置にすることとした。また、浄水装置の下流側配管に添加する銀の量を、10μg/リットル以上100μg/リットル以下に制御する銀添加装置を付加した浄水装置にすることとした。また、浄水装置から浄水装置の下流側配管に銀を10μg/リットル以上添加する機構を備えた浄水装置にすることとした。また、、浄水装置から浄水装置の下流側配管に銀を10μg/リットル以上100μg/リットル以下に制御した浄水装置にすることとした。 た め In order to solve the above-mentioned problems, the present invention provides a water purification device in which a silver addition device for adding 10 μg / liter or more of silver is added to a downstream pipe of the water purification device. Further, the water purification device was provided with a silver addition device for controlling the amount of silver added to the downstream pipe of the water purification device to be 10 μg / L or more and 100 μg / L or less. In addition, a water purifier equipped with a mechanism for adding 10 μg / liter or more of silver from the water purifier to the downstream pipe of the water purifier is adopted. In addition, a water purification apparatus was used in which silver was controlled at 10 μg / L or more and 100 μg / L or less from the water purification apparatus to the downstream pipe of the water purification apparatus.

 図2に、厚生省の指定する指定検査機関に依頼して行った大腸菌に対する銀の殺菌性能の測定結果を示す。図2より、銀の濃度が10μg/リットル以上であれば24時間を経過した滞留水に対しても十分な殺菌性能を示すことがわかる。また、銀は古くから食器やスプーンなどに使用されており、安全性が高く、味覚に与える影響もほとんど皆無である。長年にわたって愛用者が多い仁丹が大量の銀をコーティングして製造されていることからも安全性については明らかであるが、規制の観点から見ると、米国環境保護局(EPA)では、水道水中に含まれる銀濃度が第2種基準において100μg/リットル以下と規定している。望ましくは、この基準に従うことが安全を確保する意味で有意義であると考える。前述のごとく銀の殺菌性能、味覚変化、安全性については問題がないので、浄水装置において、浄水装置の下流側配管に銀を10μg/リットル以上添加する銀添加装置を付加もしくは浄水装置内にそのような機構を組み込めば、浄水装置下流の配管内でも制菌効果を得ることができ、安全で味覚の優れた浄水を提供することができる。加えて、望ましくは、米国環境保護局(EPA)で規定されている水道水中の銀濃度100μg/リットル以下の範囲で銀濃度を制御すれば、浄水装置の安全性はより高まることとなる。 Fig. 2 shows the measurement results of the sterilization performance of silver against Escherichia coli, which was performed at a designated laboratory specified by the Ministry of Health and Welfare. From FIG. 2, it can be seen that when the silver concentration is 10 μg / liter or more, sufficient sterilization performance is exhibited even for staying water after 24 hours. Silver has been used for tableware and spoons for a long time, has high safety, and has almost no effect on taste. The safety is clear from the fact that Nittan, which has been a favorite for many years, is manufactured by coating a large amount of silver, but from a regulatory perspective, the United States Environmental Protection Agency (EPA) states that The concentration of silver contained is specified to be 100 μg / liter or less based on the type 2 standard. Desirably, following this standard is considered significant in terms of ensuring safety. As described above, there is no problem with the sterilizing performance, taste change, and safety of silver. Therefore, in the water purification device, a silver addition device for adding 10 μg / liter or more of silver to the downstream pipe of the water purification device is added or installed in the water purification device. By incorporating such a mechanism, a bacteriostatic effect can be obtained even in the piping downstream of the water purification device, and safe and excellent taste-purified water can be provided. In addition, if the silver concentration is desirably controlled within the range of 100 μg / liter or less in tap water specified by the United States Environmental Protection Agency (EPA), the safety of the water purification device will be further enhanced.

 以上述べたように、本発明によれば浄水装置において、味覚の低下を招いたり昇温により発ガン性物質を生成する危険性のある塩素を添加することなく、浄水装置の下流側配管の滞留水に対して安全で効果的な制菌方法を提供することができる。 As described above, according to the present invention, in the water purifier, without adding chlorine that may cause a decrease in taste or generate a carcinogenic substance due to a rise in temperature, the retention of the downstream pipe of the water purifier can be prevented. A safe and effective bacteriostatic method for water can be provided.

 以下、本発明の具体的実施例を図に基づいて説明する。 Hereinafter, specific embodiments of the present invention will be described with reference to the drawings.

 図1に本発明の第1の実施例の構成概要を示し、以下第1の実施例について述べる。塩素やかび臭、トリハロメタンなどの有害物質を含んだ10水道水は、先ず1浄水器を通過する。浄水器には通常活性炭や不織布、あるいは中空糸膜などが使用されており、水中の濁度成分や塩素などの化学物質を分解あるいは除去する。1浄水器により浄化された10水道水は、1浄水器の下流側で銀溶出システムへと導かれる系とそのまま蛇口まで流れる系の2方向に分けられる。銀溶出システムは全体を9制御ユニットが制御する。9制御ユニットには、8流量計にて計測した蛇口方向へと流れる11浄化水の瞬時流量が与えられ、制御ユニットは4銀溶出タンクに蓄えられた14銀溶液の添加量を決定して7定量吐出ポンプに14銀溶液の吐出量を指令し、7定量吐出ポンプから14銀溶液が浄水側に吐出されて11浄化水中に適度な銀を添加する。本例では、14銀溶液の銀濃度を検出するセンサーを付加していないので、11浄化水中の銀濃度は14銀溶液の濃度を一定値とみなし、11浄化水の流量のみに応じた14銀溶液の添加による制御方式になっている。また、4銀溶出タンクには5水位検出装置が取り付けられており、4銀溶出タンクの水位情報を9制御ユニットに送っている。9制御ユニットは、4銀溶出タンクの水位が一定値以下になると2電磁弁に指令を与え、2電磁弁は自動的に弁を調整して4銀溶出タンクに浄水を補給する。 FIG. 1 shows a schematic configuration of a first embodiment of the present invention, and the first embodiment will be described below. First, 10 tap waters containing harmful substances such as chlorine, musty odor, and trihalomethane pass through one water purifier. Activated carbon, nonwoven fabric, or hollow fiber membranes are usually used in water purifiers to decompose or remove turbidity components and chemical substances such as chlorine in water. The 10 tap water purified by one water purifier is divided into two directions, a system guided to the silver elution system downstream of the one water purifier and a system directly flowing to the faucet. The silver elution system is controlled entirely by 9 control units. The control unit 9 is provided with an instantaneous flow rate of purified water 11 flowing in the direction of the faucet measured by the flow meter 8. The control unit 4 determines the amount of the silver solution 14 stored in the silver elution tank and determines the amount 7. The discharge amount of the 14 silver solution is instructed to the fixed amount discharge pump, and the 14 silver solution is discharged from the 7 fixed amount discharge pump to the purified water side to add appropriate silver to the 11 purified water. In this example, since a sensor for detecting the silver concentration of the 14 silver solution is not added, the silver concentration of the 11 purified water is regarded as a constant value of the 14 silver solution, and the silver concentration of the 14 silver solution is determined only by the flow rate of the 11 purified water. It is controlled by adding a solution. A 5 silver level detector is attached to the 4 silver elution tank, and sends the water level information of the 4 silver elution tank to 9 control units. The 9 control unit gives a command to the 2 electromagnetic valves when the water level of the 4 silver elution tank falls below a certain value, and the 2 electromagnetic valves automatically adjust the valves to supply purified water to the 4 silver elution tank.

 ここで、銀溶出の仕組みを詳述する。4銀溶出タンクの内部には微細化された固形の酸化銀と浄水が入っている。固形の銀化合物は極めて長い時間水中に浸漬すると水中にその飽和溶解度相当の銀を溶出することができる。しかしながら、本例では先に述べたように4銀溶出タンクに貯えられた14銀溶液を11浄化水に添加するので、使用者の使用状況によっては14銀溶液が短時間の間に使われ、14銀溶液を作るための浄水が補給されて14銀溶液の濃度が低下することがある。本例では、先に述べたように14銀溶液の銀濃度を検知する手段を講じていないので、14銀溶液の銀濃度を一定とみなせることが必要である。従って、14銀溶液の銀濃度を比較的早い時間で安定させることが必要であり、そのためには、飽和溶解度相当まで銀を早急に溶解することが必要になる。そこで、この固形銀化合物と浄水が入った4銀溶出タンクに超音波を与え強制的に振動させて、効率よく銀を溶解させる。4銀溶出タンク内の14銀溶液の銀濃度は酸化銀の飽和溶解度に達すると振動を与えてもそれ以上上昇することがなく、一定の上限値濃度で銀の濃度は安定する。従って、本例で示すシステムにおいても銀濃度の安定した14銀溶液を11浄化水に添加することができる。 Here, the mechanism of silver elution will be described in detail. The inside of the 4-silver elution tank contains finely divided solid silver oxide and purified water. When a solid silver compound is immersed in water for an extremely long time, silver equivalent to its saturated solubility can be eluted in water. However, in this example, since the 14 silver solution stored in the 4 silver elution tank is added to the 11 purified water as described above, the 14 silver solution is used in a short time depending on the use situation of the user, Purified water to make the 14 silver solution may be replenished and reduce the concentration of the 14 silver solution. In this example, since the means for detecting the silver concentration of the 14 silver solution is not taken as described above, it is necessary that the silver concentration of the 14 silver solution can be regarded as constant. Therefore, it is necessary to stabilize the silver concentration of the 14 silver solution in a relatively short period of time, and for that purpose, it is necessary to dissolve silver rapidly to the saturation solubility. Therefore, ultrasonic waves are applied to the 4-silver elution tank containing the solid silver compound and purified water to forcibly vibrate, thereby dissolving silver efficiently. When the silver concentration of the 14 silver solution in the 4 silver elution tank reaches the saturation solubility of silver oxide, it does not increase any more even when vibration is applied, and the silver concentration is stabilized at a certain upper limit concentration. Therefore, also in the system shown in this example, a 14 silver solution having a stable silver concentration can be added to 11 purified water.

 図3に、本発明の第2の実施例の構成概要断面図を示す。図3はいわゆるアウトインタイプの浄水器で、15筐体の内部に濾材として18銀添着活性炭が入れられている。16水道水入口から入った被処理水(必ずしも水道水である必要はない)は15筐体と20仕切の間を通過しながら18銀添着活性炭内部へと進み、中央に設けられた21中央水路から17浄化水出口を経て使用者に供給される。従来、銀添着活性炭は浄水器内部、特に微生物の発生しやすい活性炭部に制菌作用をもたせるために使用されている。従って、通常は銀を活性炭に担持し、活性炭との重量比0.1%程度の銀を活性炭部に混入しているが、この状態では浄水器の下流側配管に溶解できる銀はせいぜい1〜3μg/リットルでしかない。従って、従来から行われている銀の混入量では浄水器下流側配管に対して十分な制菌作用を持たせることができない。本実施例では、活性炭部に対する銀の混入量を増加し、活性炭との重量比で4%以上の銀を、活性炭に担持したものを用いて混入した。その結果、浄水器下流側配管内において従来1〜3μg/リットルの銀を溶出していた状態から、通水直後には120μg/リットルの銀濃度を検出し、その後徐々に銀濃度は低下してほぼ20μg/リットルの値で安定して通水できることが確認できた。 FIG. 3 shows a schematic cross-sectional view of the configuration of the second embodiment of the present invention. FIG. 3 shows a so-called out-in type water purifier in which 18 silver-impregnated activated carbon is put as a filter material in 15 cases. The water to be treated (not necessarily tap water) entering from the 16 tap water inlet passes between the 15 housings and the 20 partitions and proceeds into the activated carbon impregnated with 18 silver, and the 21 central water channel provided in the center To 17 through a purified water outlet. Conventionally, activated carbon impregnated with silver has been used to impart a bacteriostatic action to the inside of a water purifier, particularly to an activated carbon portion where microorganisms are easily generated. Therefore, normally, silver is supported on activated carbon, and silver having a weight ratio of about 0.1% to activated carbon is mixed in the activated carbon portion. In this state, silver which can be dissolved in the downstream pipe of the water purifier is at most 1 to 1. Only 3 μg / liter. Therefore, the conventional amount of silver contamination cannot provide a sufficient bacteriostatic effect on the downstream pipe of the water purifier. In the present example, the amount of silver mixed into the activated carbon part was increased, and silver having a weight ratio of 4% or more with the activated carbon was mixed using activated carbon. As a result, the silver concentration of 120 μg / liter was detected immediately after passing water from the state where silver of 1 to 3 μg / liter was conventionally eluted in the downstream pipe of the water purifier, and thereafter the silver concentration gradually decreased. It was confirmed that water could be stably passed at a value of about 20 μg / liter.

 ここで、通水直後であっても120μg/リットルの銀の溶出は、米国EPAが推奨する100μg/リットル以下を越えている。望ましくは通水直後から100μg/リットル以下の銀濃度を溶出させることであり、その方法として、活性炭との重量比で4%以上の銀を、活性炭に担持したものを浄水器に充填する前の段階で清浄な水を用いて洗浄し、乾燥してから充填した。その結果、通水直後から浄水器の下流側配管内では80μg/リットルの銀濃度であることを確認した。更に、活性炭充填前の銀を担持した活性炭の洗浄に要する時間を短縮し、あるいは通水開始直後の銀濃度を制御する方法として、洗浄に用いる浄水を昇温することも有効な手段であることを確認した。 Here, the elution of silver of 120 μg / liter even immediately after passing water exceeds 100 μg / liter or less recommended by US EPA. Desirably, a silver concentration of 100 μg / liter or less is eluted immediately after the water is passed. As a method, silver having a weight ratio of 4% or more with activated carbon and loaded on activated carbon before filling into a water purifier is used. The steps were washed with clean water, dried and filled. As a result, it was confirmed that the silver concentration was 80 μg / liter in the downstream pipe of the water purifier immediately after the passage of water. Further, as a method of shortening the time required for washing the activated carbon carrying silver before filling with activated carbon or controlling the silver concentration immediately after starting the passage of water, raising the temperature of purified water used for washing is also an effective means. It was confirmed.

銀添加装置を付加した浄水装置構成概要Outline of water purification system with silver addition device 銀による大腸菌の殺菌作用データEscherichia coli bactericidal action data by silver 銀添活性炭を用いた銀溶出機能付き浄水器の構成概要Outline of configuration of water purifier with silver elution function using silver activated carbon

符号の説明Explanation of reference numerals

1 浄水器
2 電磁弁
3 逆止弁
4 銀溶出タンク
5 水位検出装置
6 超音波振動装置
7 定量吐出ポンプ
8 流量計
9 制御ユニット
10 水道水
11 浄化水
12 制御信号
13 検出信号
14 銀溶液
15 筐体
16 水道水入口
17 浄化水出口
18 銀添着活性炭
19 水流
20 仕切
21 中央水路
DESCRIPTION OF SYMBOLS 1 Water purifier 2 Solenoid valve 3 Check valve 4 Silver elution tank 5 Water level detection device 6 Ultrasonic vibration device 7 Discharge pump 8 Flow meter 9 Control unit 10 Tap water 11 Purified water 12 Control signal 13 Detection signal 14 Silver solution 15 Case Body 16 Tap water inlet 17 Purified water outlet 18 Silver-impregnated activated carbon 19 Water flow 20 Partition 21 Central waterway

Claims (4)

塩素を除去する機能を持つ浄水装置のうち、配管の途中に切り込んで設置する浄水装置において、
 浄水装置の下流側配管に銀を10μg/リットル以上添加する銀添加装置を付加したことを特徴とする浄水装置。
Of the water purifiers that have the function of removing chlorine,
A water purifier characterized by adding a silver addition device for adding 10 μg / liter or more of silver to a downstream pipe of the water purifier.
請求項1の範囲において、
 浄水装置の下流側配管に添加する銀を10μg/リットル以上100μg/リットル以下に制御した浄水装置。
In the scope of claim 1,
A water purification device in which silver added to a downstream pipe of the water purification device is controlled to 10 μg / liter or more and 100 μg / liter or less.
塩素を除去する機能を持つ浄水装置のうち、配管の途中に切り込んで設置する浄水装置において、
 浄水装置から浄水装置の下流側配管に銀を10μg/リットル以上添加する機構を備えた浄水装置。
Of the water purifiers that have the function of removing chlorine,
A water purifier equipped with a mechanism for adding 10 μg / L or more of silver from a water purifier to a downstream pipe of the water purifier.
請求項3の範囲において、
 浄水装置の下流側に添加する銀を10μg/リットル以上100μg/リットル以下に制御した浄水装置。
In the scope of claim 3,
A water purification device in which silver added to the downstream side of the water purification device is controlled to 10 μg / liter or more and 100 μg / liter or less.
JP2003286852A 2003-08-05 2003-08-05 Water purification apparatus Pending JP2004000989A (en)

Priority Applications (1)

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JP2003286852A JP2004000989A (en) 2003-08-05 2003-08-05 Water purification apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003286852A JP2004000989A (en) 2003-08-05 2003-08-05 Water purification apparatus

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP22763697A Division JPH1157691A (en) 1997-08-07 1997-08-07 In-line type water purification facility

Publications (1)

Publication Number Publication Date
JP2004000989A true JP2004000989A (en) 2004-01-08

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Family Applications (1)

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JP2003286852A Pending JP2004000989A (en) 2003-08-05 2003-08-05 Water purification apparatus

Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20170361354A1 (en) * 2014-12-11 2017-12-21 The Regents Of The University Of Michigan Organic vapor phase deposition system and methods of use for simultaneous deposition of low and high evaporation temperature materials, and devices produced therein

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20170361354A1 (en) * 2014-12-11 2017-12-21 The Regents Of The University Of Michigan Organic vapor phase deposition system and methods of use for simultaneous deposition of low and high evaporation temperature materials, and devices produced therein

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