JP2010000433A - Apparatus for producing refined water and method for sterilizing the same - Google Patents
Apparatus for producing refined water and method for sterilizing the same Download PDFInfo
- Publication number
- JP2010000433A JP2010000433A JP2008160366A JP2008160366A JP2010000433A JP 2010000433 A JP2010000433 A JP 2010000433A JP 2008160366 A JP2008160366 A JP 2008160366A JP 2008160366 A JP2008160366 A JP 2008160366A JP 2010000433 A JP2010000433 A JP 2010000433A
- Authority
- JP
- Japan
- Prior art keywords
- purified water
- water
- treatment unit
- heated
- temperature
- 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.)
- Granted
Links
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
この発明は、精製水、特に人工透析に用いられる透析水に適した精製水の製造装置とその殺菌方法に関するものであって、精製水製造技術に属するものである。
The present invention relates to a purified water production apparatus suitable for purified water, particularly dialysis water used for artificial dialysis, and a sterilization method thereof, and belongs to purified water production technology.
市水等から不純物を、逆浸透膜を用いて除去精製して得られる精製水あるいは純水は、食料品や飲料の製造、さらには精製度を上げたものが、医療用として、また、人工透析用水として用いられている。
この医療あるいは人工透析用としての精製水は、従来、逆浸透膜処理のみにより製造されていたが、最近になって、より精製度を上げたものが求められるようになって、逆浸透膜処理に、その他の処理、例えば、ナノ膜処理、イオン交換処理などが併用されるようになってきている。
Purified water or pure water obtained by removing and purifying impurities from city water using a reverse osmosis membrane is used for the manufacture of foodstuffs and beverages, and has a higher degree of purification. Used as dialysis water.
Purified water for medical or artificial dialysis has been manufactured only by reverse osmosis membrane treatment, but recently, water with a higher degree of purification has been required. In addition, other treatments such as nano membrane treatment and ion exchange treatment have come to be used together.
一方、精製水の製造においては、市水等から混入、あるいは精製水の製造装置に付着ないしガスケットなどから侵入する各種の菌類、特にシュードモナスなどのグラム陰性菌などの棲息を抑え、無菌状態にすることが望まれている。 On the other hand, in the production of purified water, sterility is achieved by suppressing the infestation of various fungi, especially gram-negative bacteria such as Pseudomonas, mixed in from city water, etc. It is hoped that.
そのための対策として、製造された精製水を加熱することで、あるいは紫外線を照射することで殺菌しているが、無菌状態の精製水を製造するためには、精製水の製造装置自体も殺菌し、清浄な状態で運転することが重要であるので、精製水の製造装置を洗浄、消毒、殺菌する方法が種々提案されている。 As a countermeasure for this, the purified water produced is sterilized by heating or by irradiating with ultraviolet rays, but in order to produce aseptic purified water, the purified water production apparatus itself is also sterilized. Since it is important to operate in a clean state, various methods for cleaning, disinfecting, and sterilizing purified water manufacturing apparatuses have been proposed.
かかる精製水の製造装置を洗浄、消毒、殺菌する方法としては、薬液を使用する方法と熱水を使用する方法が、一般的な方法として挙げられる。
しかしながら、薬液の使用は、精製水の製造装置の劣化や環境への影響などに問題があるので、最近は、熱水、特に加熱精製水を使用する方法が主流となっている。
As a method for cleaning, disinfecting, and sterilizing such a purified water production apparatus, a general method includes a method using a chemical solution and a method using hot water.
However, the use of a chemical solution has problems in degradation of purified water production equipment and environmental impact, and recently, a method using hot water, particularly heated purified water, has become mainstream.
たとえば、特開２００４−４９９７７号公報（特許文献１）では、加熱装置により作成した温度６０℃以上７５℃未満の高温水を、逆浸透膜分離モジュール部に供給するとともに、膜分離モジュール部の精製水管路と濃縮水管路のそれぞれに、加熱装置と連通する分岐管路を設けることによって、前記高温水を、分岐管路を介して循環せしめ、逆浸透膜モジュールを高温水消毒する方法が提案されている。 For example, in Japanese Patent Application Laid-Open No. 2004-49977 (Patent Document 1), high-temperature water having a temperature of 60 ° C. or more and less than 75 ° C. created by a heating device is supplied to the reverse osmosis membrane separation module unit and the membrane separation module unit is purified. A method of disinfecting the reverse osmosis membrane module with high-temperature water by circulating the high-temperature water through the branch pipe by providing a branch pipe communicating with the heating device in each of the water pipe and the concentrated water pipe is proposed. ing.
また、特開２００４−７４１０９号公報（特許文献２）においては、原料水を逆浸透膜装置および電気再生式純水製造装置をこの順に備えた系で処理し、医薬品用精製水を製造する装置を、この装置で得た処理原料水を加熱しつつ系内に循環させることにより、系内を殺菌する方法が提案されている。 In addition, in Japanese Patent Application Laid-Open No. 2004-74109 (Patent Document 2), an apparatus for producing purified water for pharmaceuticals by treating raw water with a system including a reverse osmosis membrane device and an electric regeneration type pure water production device in this order. Has been proposed to sterilize the inside of the system by circulating the raw material water obtained with this apparatus while heating it in the system.
さらに、特開２００７−１４３８２２号公報（特許文献３）では、複数の水処理機器からなり、飲料又は食品の製造に用いられる純水を、原料水から製造する純水製造装置を、１又は複数の水処理機器の単位に分割し、分割された単位ごとに、異なった水質および／または異なった頻度で加熱精製水殺菌する方法が提案されている。
上記の特許文献１や特許文献２に記載された方法は、熱水、特に加熱精製水を、処理部全体に循環して殺菌を行なうというものである。
したがって、装置も操作も単純で、取り扱い易い方法であるが、併用される処理部が増加すると、殺菌時間が長くなり、必要な熱量も多量になって、処理部が増加した装置では、使用し難いという問題を有するものである。
The methods described in Patent Document 1 and Patent Document 2 described above are sterilized by circulating hot water, particularly heated purified water, throughout the entire processing unit.
Therefore, the device and operation are simple and easy to handle, but if the number of treatment units used increases, the sterilization time becomes longer, the amount of heat required increases, and the device with more treatment units is used. It has a problem that it is difficult.
また、特許文献３に記載の方法は、本質的に処理部ごとに殺菌を施すものである。
したがって、その処理部に適した殺菌条件、すなわち、熱水の温度や添加薬剤の種類や量を処理部に応じて変化させることができる点で優れているが、装置全体が複雑になるとともに、操作も簡便でないという問題を有するものである。
The method described in Patent Document 3 essentially sterilizes each processing unit.
Therefore, the sterilization conditions suitable for the processing unit, that is, the temperature and the kind and amount of the additive chemical of hot water can be changed according to the processing unit, but the entire apparatus becomes complicated, The operation is not easy.
この発明はかかる現状に鑑み、熱水による殺菌処理を、特定の処理部だけでなく、精製水の製造装置全体を対象とし、しかも処理時間を少しでも短縮し、系内に生ずる放熱を最小限に抑えることを種々検討した。 In view of the present situation, the present invention is intended for sterilization treatment with hot water not only for a specific treatment section but also for the entire purified water production apparatus, further shortening the treatment time, and minimizing heat dissipation generated in the system. Various investigations were made to keep it at a minimum.
その結果、精製水を加熱して得られる加熱精製水を、複数存在する処理部の上流側の処理部から下流に存在する処理部に一括して循環させるとともに、上流側の処理部から順次殺菌を完了させ、殺菌の完了した処理部への加熱精製水の通水を停止するという方法を採用することにより、解決し得ることを見出し、この発明を完成させたものである。 As a result, the heated purified water obtained by heating the purified water is circulated from the upstream processing unit to the downstream processing unit, and sterilized sequentially from the upstream processing unit. The present invention has been completed by finding that it can be solved by adopting a method of stopping the flow of heated and purified water to the processing section that has been sterilized.
すなわち、この発明は、精製水の製造装置の熱水殺菌を、より効率よく行なうことができるとともに、殺菌処理の要する時間を短縮し、加熱精製水を得るのに使用する熱エネルギーを減少させ、経済的にも環境的にも優れた精製水の製造方法を提供すること、またそのための装置を提供することを目的とするものである。
That is, this invention can perform hot water sterilization of purified water production apparatus more efficiently, shorten the time required for sterilization treatment, reduce the thermal energy used to obtain heated purified water, An object of the present invention is to provide a method for producing purified water that is economically and environmentally superior, and to provide an apparatus therefor.
前記の目的を達成するため、この発明の請求項１に記載の発明は、
原料水供給槽を上流とし、上流側から活性炭処理部、ナノ透過膜処理部、逆浸透膜処理部およびそれらの処理部で処理され製造された精製水を貯留する精製水貯留槽を主要構成要素とし、
前記精製水貯留槽は加熱手段を具備し、
前記加熱手段によって加熱された精製水を、前記各処理部に送液を可能とするバイパス主管と、
前記バイパス主管から分岐し、前記加熱精製水を、前記各処理部の上流側に個別に送液するバイパス支管が配設されていること
を特徴とする精製水製造装置である。
In order to achieve the above object, the invention according to claim 1 of the present invention provides:
Main components are the raw water supply tank upstream, and the purified water storage tank that stores the purified water processed and manufactured from the activated carbon processing section, nano-permeable membrane processing section, reverse osmosis membrane processing section and those processing sections from the upstream side age,
The purified water storage tank comprises heating means,
A bypass main pipe that enables the purified water heated by the heating means to be sent to the processing sections,
A purified water production apparatus characterized in that a bypass branch pipe is provided that branches from the bypass main pipe and individually feeds the heated purified water to the upstream side of each processing section.
また、この発明の請求項２に記載の発明は、
原料水供給槽を上流とし、上流側から活性炭処理部、ナノ透過膜処理部、逆浸透膜処理部およびそれらの処理部で処理され製造された精製水を貯留する精製水貯留槽を主要構成要素とし、
前記精製水貯留槽は加熱手段を具備し、
前記加熱手段によって加熱された精製水を、前記各処理部に送液を可能とするバイパス主管と、
前記バイパス主管から分岐し、前記加熱精製水を、前記各処理部の上流側に個別に送液するバイパス支管が配設されたもので、
前記最上流側に位置するバイパス支管を経て、最上流側の処理部から下流側の各処理部へ前記加熱精製水を循環させ、最上流側の処理部通過した加熱精製水の温度が所定温度以上に達し、かつその温度が所定時間維持されたとき、当該バイパス支管への送液が停止され、当該処理部の下流側に位置するバイパス支管を経て、次の処理部以降に加熱精製水が送液され、爾後同様の動作を順次繰り返すことによって、主要構成要素の殺菌が施されるよう構成されていること
を特徴とする精製水製造装置である。
The invention according to claim 2 of the present invention is
Main components are the raw water supply tank upstream, and the purified water storage tank that stores the purified water processed and manufactured from the activated carbon processing section, nano-permeable membrane processing section, reverse osmosis membrane processing section and those processing sections from the upstream side age,
The purified water storage tank comprises heating means,
A bypass main pipe that enables the purified water heated by the heating means to be sent to the processing sections,
A bypass branch pipe branched from the bypass main pipe and supplying the heated purified water individually to the upstream side of each processing section is provided,
Through the bypass branch located on the most upstream side, the heated purified water is circulated from the most upstream processing unit to each downstream processing unit, and the temperature of the heated purified water passing through the most upstream processing unit is a predetermined temperature. When the temperature reaches the above and the temperature is maintained for a predetermined time, the liquid feeding to the bypass branch is stopped, and the heated purified water is supplied to the subsequent processing section after the bypass branch located on the downstream side of the processing section. The purified water production apparatus is characterized in that the main components are sterilized by sequentially repeating the same operation after the liquid is fed and after dripping.
また、この発明の請求項３に記載の発明は、
請求項１又は２に記載の精製水製造装置において、
前記バイパス主管およびバイパス支管は、
各処理部における原料水ないし中間処理水のバイパス管としての利用可能に配設されていること
を特徴とするものである。
The invention according to claim 3 of the present invention is
In the purified water manufacturing apparatus according to claim 1 or 2,
The bypass main pipe and the bypass branch pipe are:
It is arranged to be usable as a bypass pipe for raw water or intermediate treated water in each treatment section.
さらに、この発明の請求項４に記載の発明は、
原料水供給槽を上流とし、精製水貯留槽を下流とし、その間に順次配置された各水処理部を用いて、原料水から精製水を製造する精製水製造装置の系内の殺菌処理に際し、
前記精製水貯留槽の精製水を加熱しながら、最上流側の水処理部に送液して、精製水製造装置内に精製水を循環させ、
最上流側の水処理部における精製水の温度が所定温度以上に達し、かつ所定時間維持されたとき、当該水処理部への加熱精製水の送液を停止し、当該水処理部の下流側に位置する水処理部に加熱精製水の送液を開始して、当該精製水製造装置の下流側で循環させ、爾後同様の動作を下流側の水処理部に実施することによって行なうこと
を特徴とする精製水製造装置の殺菌方法である。
Further, the invention according to claim 4 of the present invention is
In the sterilization treatment in the system of the purified water production apparatus that produces purified water from the raw water using each water treatment unit arranged sequentially between the raw water supply tank upstream and the purified water storage tank downstream,
While heating the purified water in the purified water storage tank, the solution is sent to the water treatment unit on the most upstream side, and the purified water is circulated in the purified water production apparatus.
When the temperature of the purified water in the uppermost stream water treatment unit reaches a predetermined temperature or more and is maintained for a predetermined time, the heating purified water feeding to the water treatment unit is stopped and the downstream side of the water treatment unit The heated water treatment unit located in the water treatment unit is started to feed heated purified water, circulates on the downstream side of the purified water production apparatus, and the same operation is performed on the downstream side water treatment unit. This is a method for sterilizing a purified water production apparatus.
また、この発明の請求項５に記載の発明は、
請求項４に記載の精製水製造装置の殺菌方法において、
前記精製水製造装置は、
少なくとも上流側から活性炭処理部、ナノ膜処理部および逆浸透膜処理部を有するものであって、
第１工程：加熱精製水を、前記活性炭処理部からナノ膜処理部および逆浸透膜処理部に順に循環させ、前記活性炭処理部の精製水の温度が、所定温度でかつ所定時間維持されたとき、前記活性炭処理部への送液を停止する工程。
第２工程：前記活性炭処理部への送液が停止されたのち、加熱精製水をナノ膜処理部から逆浸透膜処理部に循環させ、前記ナノ膜処理部の精製水の温度が、所定温度でかつ所定時間維持されたとき、前記ナノ膜処理部への送液を停止する工程。
第３工程：前記ナノ膜処理槽への送液が停止されたのち、加熱精製水を逆浸透膜処理部に循環させ、前記逆浸透膜処理部の精製水の温度が、所定温度でかつ所定時間維持されたとき、前記逆浸透膜処理槽への送液を停止する工程。
を順次実施すること
を特徴とするものである。
The invention according to claim 5 of the present invention is
In the purification method of the purified water manufacturing apparatus of Claim 4,
The purified water production apparatus is
It has at least an activated carbon treatment part, a nano membrane treatment part and a reverse osmosis membrane treatment part from the upstream side,
First step: When heated purified water is circulated in order from the activated carbon treatment unit to the nano membrane treatment unit and the reverse osmosis membrane treatment unit, and the temperature of the purified water in the activated carbon treatment unit is maintained at a predetermined temperature for a predetermined time. The process of stopping liquid feeding to the activated carbon treatment part.
Second step: After the liquid supply to the activated carbon treatment unit is stopped, the heated purified water is circulated from the nano membrane treatment unit to the reverse osmosis membrane treatment unit, and the temperature of the purified water in the nano membrane treatment unit is a predetermined temperature. And, when maintained for a predetermined time, stopping the liquid feeding to the nanofilm processing section.
Third step: After the liquid feeding to the nano membrane treatment tank is stopped, the heated purified water is circulated to the reverse osmosis membrane treatment unit, and the temperature of the purified water in the reverse osmosis membrane treatment unit is a predetermined temperature and a predetermined value. A step of stopping liquid feeding to the reverse osmosis membrane treatment tank when the time is maintained.
Are sequentially performed.
また、この発明の請求項６に記載の発明は、
請求項４又は５に記載の精製水製造装置の殺菌方法において、
前記各処理部の殺菌は、
処理部内温度を、少なくとも温度８０℃以上に保持することにより行なうこと
を特徴とするものである。
The invention according to claim 6 of the present invention provides
In the sterilization method of the purified water manufacturing apparatus according to claim 4 or 5,
The sterilization of each processing unit is
This is performed by maintaining the temperature in the processing section at least at a temperature of 80 ° C. or higher.
また、この発明の請求項７に記載の発明は、
請求項６に記載の精製水製造装置の殺菌方法において、
前記保持時間は、
１〜６０分であること
を特徴とするものである。
The invention according to claim 7 of the present invention provides
In the sterilization method of the purified water manufacturing apparatus according to claim 6,
The holding time is
1 to 60 minutes.
また、この発明の請求項８に記載の発明は、
請求項４に記載の精製水製造装置の殺菌方法において、
前記精製水の循環は、
常温状態の精製水の加熱開始と同時に、又は加熱によって精製水の温度を、所定温度に昇温中に開始させること
を特徴とするものである。
The invention according to claim 8 of the present invention provides
In the purification method of the purified water manufacturing apparatus of Claim 4,
The purified water circulation is
The temperature of the purified water is started at the same time as the heating of the purified water at room temperature or by heating to a predetermined temperature.
また、この発明の請求項９に記載の発明は、
請求項４又は５に記載の精製水製造装置の殺菌方法において、
加熱された精製水による殺菌完了後、原料水を用いて、加温された各処理部を冷却し、冷却に用いられた原料水は系外に排出する工程を有すること
を特徴とするものである。
The invention according to claim 9 of the present invention provides
In the sterilization method of the purified water manufacturing apparatus according to claim 4 or 5,
After completion of sterilization with heated purified water, the raw water is used to cool each heated processing section, and the raw water used for cooling is discharged outside the system. is there.
この発明の精製水製造装置の殺菌法は、殺菌すべき処理部の全てに加熱精製水を循環させて、精製水製造装置全体を殺菌するという方式であるため、精製水製造装置が複雑化せず、操作も簡便という優れたものである。
さらに、上流に存在する処理部から流れに沿って加熱精製水を循環させ、殺菌の完了した上流の処理部から順次加熱精製水の循環を終了させることによって、殺菌処理のための時間の短縮化が図られ、結果として、加熱精製水を一定温度に維持する熱量を削減でき、省力的にも大きな貢献をもたらすものである。
The sterilization method of the purified water production apparatus according to the present invention is a system in which heated purified water is circulated through all the processing parts to be sterilized to sterilize the entire purified water production apparatus. In addition, the operation is excellent and simple.
Furthermore, shortening the time for sterilization treatment by circulating heated purified water along the flow from the upstream processing unit and ending the circulation of heated purified water sequentially from the upstream processing unit that has been sterilized As a result, the amount of heat for maintaining the heated and purified water at a constant temperature can be reduced, and this contributes greatly to labor saving.
さらに、各処理部に加熱精製水を供給する配管を、各処理部のバイパスとして利用することができ、必要に応じて、殺菌されたバイパスとして有効に利用することができるという効果も奏するものである。
Furthermore, the piping for supplying heated purified water to each processing unit can be used as a bypass for each processing unit, and if necessary, it can also be effectively used as a sterilized bypass. is there.
以下、この発明の精製水製造装置およびその殺菌方法について、添付の図面を基づいて詳細に説明する。
なお、この発明は実施例にのみ限定されるものではなく、発明の要旨を変更しない範囲内において種々変更を加えることができるものである。
Hereinafter, the purified water production apparatus and the sterilization method of the present invention will be described in detail with reference to the accompanying drawings.
In addition, this invention is not limited only to an Example, A various change can be added in the range which does not change the summary of invention.
この発明にかかる精製水製造装置は、図１に示すように、原料水供給槽１、カーボンフィルタ濾過処理槽３、ナノ透過膜処理槽４、逆浸透膜処理槽５および精製水貯留槽６を主要構成要素とするものである。 As shown in FIG. 1, the purified water production apparatus according to the present invention includes a raw water supply tank 1, a carbon filter filtration treatment tank 3, a nano-permeable membrane treatment tank 4, a reverse osmosis membrane treatment tank 5, and a purified water storage tank 6. The main component.
原料水は、図１の濃線に示されるように、原料水供給槽１からインバータ制御されるポンプ８ａによって１０μ径の細孔を有する原料水フィルタ槽２に送られて、原料水中の比較的細かい濁質（１０μ以上）を除去したのち、カーボンフィルタ濾過処理槽３に送られる。
このカーボンフィルタ濾過処理槽３に送られた原料水は、原料水（水道水）中に含まれる塩素を活性炭で吸着除去したのち、ポンプ８ｂによって加圧されながらナノ透過膜処理槽４に送られる。
As shown by the dark line in FIG. 1, the raw water is sent from the raw water supply tank 1 to the raw water filter tank 2 having pores with a diameter of 10 μm by a pump 8a controlled by an inverter, After removing fine turbidity (10 μm or more), it is sent to the carbon filter filtration treatment tank 3.
The raw water sent to the carbon filter filtration tank 3 is sent to the nano-permeable membrane treatment tank 4 while being pressurized by the pump 8b after adsorbing and removing chlorine contained in the raw water (tap water) with activated carbon. .
このナノ透過膜処理槽４においては、原料水中に含まれる金属イオン類を一次除去すると同時に、バクテリア等の有機物も除去されたのち、インバータ制御されるポンプ８ｃによって加圧されながら、逆浸透膜処理槽５に送られる。 In this nano-permeable membrane treatment tank 4, the metal ions contained in the raw water are primarily removed, and at the same time, organic substances such as bacteria are removed, and then the reverse osmosis membrane treatment is performed while being pressurized by the inverter-controlled pump 8 c. It is sent to the tank 5.
前記逆浸透膜処理槽５においては、さらに金属イオン類やバクテリア等の有機物が除去されたのち、精製水貯留槽６において貯えられ、必要に応じて、同じくポンプ８ｄにより透析装置１０などに供給される。 In the reverse osmosis membrane treatment tank 5, organic substances such as metal ions and bacteria are further removed, and then stored in the purified water storage tank 6 and supplied to the dialyzer 10 and the like by the pump 8 d as necessary. The
このような精製水製造装置によって製造される、透析用などの医療用水などとして使用される精製水は、その品質について、厳しい規格、特にエンドトキシンなどを産生する生菌についての規格が存在する。
したがって、得られた精製水の品質は常に監視され、その品質に異常が認められた際、あるいは精製水製造装置の生菌による汚染を考慮しなければならない状態に至った時、さらには定期的に、精製水製造装置の殺菌が行われている。
There is a strict standard for the quality of purified water produced by such a purified water production apparatus and used as medical water for dialysis and the like, particularly for live bacteria that produce endotoxin and the like.
Therefore, the quality of the purified water obtained is constantly monitored, and when there is an abnormality in the quality, or when it becomes necessary to take into account the contamination of the purified water production equipment by viable bacteria, and regularly In addition, the purified water production apparatus is sterilized.
この発明の精製水製造装置においては、その殺菌を加熱精製水で行なうに適した装置とするため、前記精製水貯留槽６には加熱装置７が付設されている。 In the purified water production apparatus of the present invention, a heating device 7 is attached to the purified water storage tank 6 in order to make the apparatus suitable for performing sterilization with heated purified water.
なお、この加熱装置７は、精製水貯留槽６内の精製水を加熱することができるものであれば、電気ヒータであっても、ボイラーであっても、熱交換方式であっても、その具体的手段には制限はないものである。
また、この加温装置７による精製水の加熱は、精製水の温度が９０℃以上に上昇したときには、加温を停止させるものである。
The heating device 7 may be an electric heater, a boiler, a heat exchange system, or the like as long as it can heat purified water in the purified water storage tank 6. There is no limitation on the specific means.
The heating of the purified water by the heating device 7 stops the heating when the temperature of the purified water rises to 90 ° C. or higher.
さらに、この発明の精製水製造装置においては、装置全体を加熱精製水によって殺菌消毒処理するために、より具体的には、微生物の増加を抑制するため、加熱した精製水を前記の各処理部に送液するためのポンプ８ｅが、前記精製水貯留槽６に付設されている。
また、前記ポンプ８ｅを介して、加熱精製水を循環させるためのバイパス主管９と、このバイパス主管９から各処理部に送液するためバイパス支管９ａ，９ｂ，９ｃが、図１に示すように配置されている。
Further, in the purified water production apparatus of the present invention, in order to sterilize and disinfect the entire apparatus with the heated purified water, more specifically, in order to suppress the increase of microorganisms, the heated purified water is treated with each of the above treatment units. The purified water storage tank 6 is provided with a pump 8e for feeding liquid.
Further, as shown in FIG. 1, a bypass main pipe 9 for circulating heated purified water through the pump 8e and bypass branch pipes 9a, 9b, 9c for sending liquid from the bypass main pipe 9 to each processing section Is arranged.
なお、前記のバイパス主管９は、原料水供給槽１に接続することによって、精製水の回収再利用に用いることができる。
また、バイパス主管９とバイパス支管９ａ，９ｂ，９ｃとのサイクルを、精製水製造時において、各処理部のバイパスとして、具体的には、
１）原料水供給槽１を介さす原料水を、バイパス主管９→バイパス支管９ａを利用してカーボンフィルタ濾過処理槽３に、
２）原料水供給槽１を介さす原料水を、バイパス主管９→バイパス支管９ｂを利用してナノ透過膜処理槽４に、
３）バイパス支管９ｂ→バイパス主管９→バイパス支管９ｃを利用して、カーボンフィルタ濾過処理槽３からの原料水を逆浸透膜処理槽５に、
４）バイパス支管９ｃ→バイパス主管９を利用して、ナノ透過膜処理槽４で処理された原料水を直接精製水貯留槽６に
５）バイパス支管９ｃ→バイパス主管９を利用して、ナノ透過膜処理槽４で処理された原料水を直接透析装置に、供給することも可能なものである。
The bypass main pipe 9 can be used for recovery and reuse of purified water by connecting to the raw water supply tank 1.
In addition, the cycle of the bypass main pipe 9 and the bypass branch pipes 9a, 9b, 9c, as a bypass of each processing unit at the time of producing purified water, specifically,
1) The raw water through the raw water supply tank 1 is transferred to the carbon filter filtration tank 3 by using the bypass main pipe 9 → the bypass branch pipe 9a.
2) Feed the raw water through the raw water supply tank 1 into the nano-permeable membrane treatment tank 4 using the bypass main pipe 9 → the bypass branch pipe 9b.
3) By using the bypass branch pipe 9b → the bypass main pipe 9 → the bypass branch pipe 9c, the raw water from the carbon filter filtration treatment tank 3 is supplied to the reverse osmosis membrane treatment tank 5;
4) Bypass branch pipe 9c → By using bypass main pipe 9, raw water treated in nano-permeable membrane treatment tank 4 is directly supplied to purified water storage tank 6 5) Bypass branch pipe 9c → By using bypass main pipe 9, nano-permeation The raw water treated in the membrane treatment tank 4 can be directly supplied to the dialysis machine.
かかる構成の精製水製造装置による消毒殺菌処理は、以下のようにして行なわれる。
消毒殺菌処理に際して、まず、精製水貯留槽６に設けられた加熱装置７を作動させ、精製水貯留槽６に貯留されている精製水を加熱する。
The disinfection and sterilization process by the purified water production apparatus having such a configuration is performed as follows.
In the disinfection and sterilization process, first, the heating device 7 provided in the purified water storage tank 6 is operated to heat the purified water stored in the purified water storage tank 6.
ついで、加熱された精製水は、前記送水ポンプ８ｅによってバイパス主管９およびバイパス支管９ａを介して、カーボンフィルタ濾過処理槽３の上流（流入）側に送られ、カーボンフィルタ濾過処理槽３→ナノ透過膜処理槽４→逆浸透膜処理槽５内を通過して、装置内を殺菌しながら精製水貯留槽６に戻るという循環流が形成される。 Next, the heated purified water is sent to the upstream (inflow) side of the carbon filter filtration tank 3 through the bypass main pipe 9 and the bypass branch pipe 9a by the water pump 8e, and the carbon filter filtration tank 3 → nano permeation. A circulation flow is formed that passes through the membrane treatment tank 4 → the reverse osmosis membrane treatment tank 5 and returns to the purified water storage tank 6 while sterilizing the inside of the apparatus.
より具体的には、精製水貯留槽６に貯留されている精製水を、カーボンフィルタ濾過処理槽３の消毒殺菌に最適な温度に設定し、加熱を開始し、精製水貯留槽６→送水ポンプ８ｅ→バイパス主管９→バイパス支管９ａ→カーボンフィルタ濾過処理槽３→ナノ透過膜処理槽４→逆浸透膜処理槽５→精製水貯留槽６の順に加熱循環を行なう。 More specifically, the purified water stored in the purified water storage tank 6 is set to an optimum temperature for disinfection and sterilization of the carbon filter filtration processing tank 3, heating is started, and the purified water storage tank 6 → water pump Heat circulation is performed in the order of 8e → bypass main pipe 9 → bypass branch pipe 9a → carbon filter filtration treatment tank 3 → nanopermeable membrane treatment tank 4 → reverse osmosis membrane treatment tank 5 → purified water storage tank 6.
そして、カーボンフィルタ濾過処理槽３の出口温度が設定温度８０℃に到達後、設定時間１０分が経過すると、カーボンフィルタ濾過処理槽３の消毒殺菌処理は完了とし、前記加熱精製水の循環経路を変更し、ナノ透過膜処理槽４の入口側に切り替え、精製水貯留槽６の加熱設定温度をナノ透過膜処理槽４の消毒殺菌に最適な温度に設定し、加熱循環を行なうものである。 When the set time of 10 minutes elapses after the outlet temperature of the carbon filter filtration treatment tank 3 reaches the set temperature of 80 ° C., the disinfection and sterilization treatment of the carbon filter filtration treatment tank 3 is completed, and the heating purified water circulation path is It changes, it switches to the entrance side of the nano permeable membrane processing tank 4, the heating preset temperature of the purified water storage tank 6 is set to the optimal temperature for disinfection sterilization of the nano permeable membrane processing tank 4, and heating circulation is performed.
ナノ透過膜処理槽４の出口温度が設定温度８０℃に到達後、設定時間３０分が経過すると、ナノ透過膜処理槽４の消毒殺菌処理は完了とし、加熱精製水の循環経路を変更し、逆浸透膜処理槽５の入口側に切り替え、精製水貯留槽６の加熱設定温度を逆浸透膜処理槽５の消毒殺菌に最適な温度に設定し、加熱循環を行なうものである。 When the set time of 30 minutes has elapsed after the outlet temperature of the nano-permeable membrane treatment tank 4 reaches the set temperature of 80 ° C., the disinfection and sterilization treatment of the nano-permeable membrane treatment tank 4 is completed, and the circulation path of the heated and purified water is changed. By switching to the inlet side of the reverse osmosis membrane treatment tank 5, the heating set temperature of the purified water storage tank 6 is set to an optimum temperature for disinfection and sterilization of the reverse osmosis membrane treatment tank 5, and heating circulation is performed.
前記逆浸透膜処理槽５の出口温度が設定温度８０℃に到達後、設定時間３０分が経過すると、逆浸透膜処理槽５の消毒殺菌処理は完了とする。 After the outlet temperature of the reverse osmosis membrane treatment tank 5 reaches the set temperature of 80 ° C., when the set time of 30 minutes elapses, the disinfection sterilization process of the reverse osmosis membrane treatment tank 5 is completed.
このように、最終的には、精製水の加熱は、精製水の温度が殺菌に必要な温度８０℃以上になるように行なわれ、その温度に加熱された精製水によって本質的に殺菌が行なわれるものである。
その際、精製水の循環は、前記精製水貯留槽６に貯留されている精製水が温度８０℃以上になる前から、すなわち、精製水の昇温中に開始することが、消毒殺菌時間の短縮のために好ましい。
Thus, finally, the purified water is heated so that the temperature of the purified water becomes 80 ° C. or higher necessary for sterilization, and sterilization is essentially performed by the purified water heated to that temperature. It is what
At that time, the circulation of the purified water starts before the purified water stored in the purified water storage tank 6 reaches a temperature of 80 ° C. or higher, that is, during the temperature increase of the purified water. Preferred for shortening.
加熱された精製水の循環による各処理部の加熱温度は、少なくとも温度８０℃以上が微生物の増殖を抑えるのに最も効果的で、その加熱時間は、処理部によって異なるが、１〜６０分、より好ましくは１０〜３０分である。 The heating temperature of each processing unit by circulating purified water is at least 80 ° C. is most effective for suppressing the growth of microorganisms, and the heating time varies depending on the processing unit, but is 1 to 60 minutes. More preferably, it is 10 to 30 minutes.
加熱精製水の逆浸透膜処理槽５と精製水貯留槽６の循環によって、逆浸透膜処理槽５の殺菌が完了したならば、加熱精製水の送液を停止し、精製水製造装置の殺菌完了とする。
なお、加熱された精製水による消毒殺菌処理に際し、精製水製造装置、特に各処理部が高温となっているので、原料水を用いて、加温された処理部を冷却する。
冷却に用いられた原料水は、系外に排出溝１１などを用いて放出する。
When the sterilization of the reverse osmosis membrane treatment tank 5 is completed by the circulation of the reverse osmosis membrane treatment tank 5 and the purified water storage tank 6 of the heated purified water, the heating purified water feed is stopped and the purified water production apparatus is sterilized. Completed.
In addition, in the disinfection sterilization process by the heated purified water, since the purified water manufacturing apparatus, especially each process part is high temperature, the heated process part is cooled using raw material water.
The raw water used for cooling is discharged out of the system using the discharge groove 11 or the like.
以上の操作による殺菌完了に要した時間は、それぞれの殺菌条件を、カーボンフィルタ濾過処理槽３について温度８０℃×１０分、ナノ透過膜処理槽４について温度８０℃×３０分、逆浸透膜処理槽５について温度８０℃×３０分とした場合、精製水貯留槽６の加温開始からで２時間４７分であった。
これに対し、加熱された精製水を、同一装置を使用して、バイパス主管９→バイパス支管９ａ→カーボンフィルタ濾過処理槽３→ナノ透過膜処理槽４→逆浸透膜処理槽５→精製水貯留槽６の順に循環させて消毒殺菌処理に要した時間は３時間１５分であったので、明らかにこの発明の消毒殺菌処理が効果的であった。
The time required for completion of sterilization by the above operation is as follows. The sterilization conditions are as follows: temperature 80 ° C. × 10 minutes for the carbon filter filtration treatment tank 3, temperature 80 ° C. × 30 minutes for the nanopermeable membrane treatment tank 4, When the temperature of the tank 5 was 80 ° C. × 30 minutes, it was 2 hours 47 minutes from the start of heating of the purified water storage tank 6.
On the other hand, the heated purified water is supplied to the bypass main pipe 9 → bypass branch 9a → carbon filter filtration treatment tank 3 → nanopermeable membrane treatment tank 4 → reverse osmosis membrane treatment tank 5 → purified water storage using the same apparatus. Since the time required for the disinfection and sterilization by circulating in the order of the tank 6 was 3 hours and 15 minutes, the disinfection and sterilization of the present invention was clearly effective.
また、放出される熱量も、精製水貯留槽６を収納するキャビネット内の温度が５９．２℃と温度５７．２℃と異なり、減少していることが認められた。 Further, it was recognized that the amount of heat released was also decreased, with the temperature in the cabinet housing the purified water storage tank 6 being 59.2 ° C. and the temperature 57.2 ° C.
なお、消毒殺菌処理に際し、加熱精製水の循環と経路の切り替えは、すべてコンピュータ制御によって実施されるもので、各ポンプもインバータ制御の可能なものを使用することが好ましい。 In the disinfection and sterilization treatment, the circulation of the heated and purified water and the switching of the route are all performed by computer control, and it is preferable to use a pump that can be controlled by an inverter.
また、この発明の精製水製造装置は、消毒殺菌処理のために、バイパス主管と複数のバイパス支管を具備しているので、逆浸透膜処理槽５のみを単独で消毒殺菌処理することも当然可能なものである。
Moreover, since the purified water production apparatus of this invention is equipped with a bypass main pipe and a plurality of bypass branch pipes for the disinfection and sterilization treatment, it is naturally possible to disinfect only the reverse osmosis membrane treatment tank 5 alone. Is something.
この発明の精製水製造装置およびその殺菌法は、消毒殺菌すべき処理部に一括して加熱精製水を循環させて、装置を消毒殺菌するという方式であるため、装置が複雑化せず、操作も簡便という優れたもので、精製水、純水などを使用する業界において広く利用される可能性の高いものである。
The purified water production apparatus and its sterilization method of the present invention is a system in which heated purified water is circulated collectively to the processing section to be disinfected and sterilized, and the apparatus is sterilized and sterilized. Is also easy to use, and is highly likely to be widely used in industries that use purified water, pure water, and the like.
１ 原料水供給槽
２ フィルタ槽
３ カーボンフィルタ濾過処理槽
４ ナノ透過膜処理槽
５ 逆浸透膜処理槽
６ 精製水貯留槽
７ 加熱装置
８ａ〜８ｅ ポンプ
９ バイパス主管
９ａ〜９ｃ バイパス支管
１０ 透析装置
１１ 排出口
DESCRIPTION OF SYMBOLS 1 Raw material water supply tank 2 Filter tank 3 Carbon filter filtration treatment tank 4 Nanopermeation membrane treatment tank 5 Reverse osmosis membrane treatment tank 6 Purified water storage tank 7 Heating device 8a-8e Pump 9 Bypass main pipe 9a-9c Bypass branch pipe 10 Dialysis apparatus 11 Vent
Claims (9)
前記精製水貯留槽は加熱手段を具備し、
前記加熱手段によって加熱された精製水を、前記各処理部に送液を可能とするバイパス主管と、
前記バイパス主管から分岐し、前記加熱精製水を、前記各処理部の上流側に個別に送液するバイパス支管が配設されていること
を特徴とする精製水製造装置。 Main components are the raw water supply tank upstream, and the purified water storage tank that stores the purified water processed and manufactured from the activated carbon processing section, nano-permeable membrane processing section, reverse osmosis membrane processing section and those processing sections from the upstream side age,
The purified water storage tank comprises heating means,
A bypass main pipe that enables the purified water heated by the heating means to be sent to the processing sections,
A purified water production apparatus, wherein a bypass branch pipe is provided that branches from the bypass main pipe and individually feeds the heated purified water to the upstream side of each processing section.
前記精製水貯留槽は加熱手段を具備し、
前記加熱手段によって加熱された精製水を、前記各処理部に送液を可能とするバイパス主管と、
前記バイパス主管から分岐し、前記加熱精製水を、前記各処理部の上流側に個別に送液するバイパス支管が配設されたもので、
前記最上流側に位置するバイパス支管を経て、最上流側の処理部から下流側の各処理部へ前記加熱精製水を循環させ、最上流側の処理部通過した加熱精製水の温度が所定温度以上に達し、かつその温度が所定時間維持されたとき、当該バイパス支管への送液が停止され、当該処理部の下流側に位置するバイパス支管を経て、次の処理部以降に加熱精製水が送液され、爾後同様の動作を順次繰り返すことによって、主要構成要素の殺菌が施されるよう構成されていること
を特徴とする精製水製造装置。 Main components are the raw water supply tank upstream, and the purified water storage tank that stores the purified water processed and manufactured from the activated carbon processing section, nano-permeable membrane processing section, reverse osmosis membrane processing section and those processing sections from the upstream side age,
The purified water storage tank comprises heating means,
A bypass main pipe that enables the purified water heated by the heating means to be sent to the processing sections,
A bypass branch pipe branched from the bypass main pipe and supplying the heated purified water individually to the upstream side of each processing section is provided,
Through the bypass branch located on the most upstream side, the heated purified water is circulated from the most upstream processing unit to each downstream processing unit, and the temperature of the heated purified water passing through the most upstream processing unit is a predetermined temperature. When the temperature reaches the above and the temperature is maintained for a predetermined time, the liquid feeding to the bypass branch is stopped, and the heated purified water is supplied to the subsequent processing section after the bypass branch located on the downstream side of the processing section. An apparatus for producing purified water, wherein the main components are sterilized by sequentially repeating the same operation after being fed and after dripping.
各処理部における原料水ないし中間処理水のバイパス管としての利用可能に配設されていること
を特徴とする請求項１又は２に記載の精製水製造装置。 The bypass main pipe and the bypass branch pipe are:
The purified water production apparatus according to claim 1 or 2, wherein the apparatus is disposed so as to be usable as a bypass pipe for raw water or intermediate treated water in each treatment section.
前記精製水貯留槽の精製水を加熱しながら、最上流側の水処理部に送液して、精製水製造装置内に精製水を循環させ、
最上流側の水処理部における精製水の温度が所定温度以上に達し、かつ所定時間維持されたとき、当該水処理部への加熱精製水の送液を停止し、当該水処理部の下流側に位置する水処理部に加熱精製水の送液を開始して、当該精製水製造装置の下流側で循環させ、爾後同様の動作を下流側の水処理部に実施することによって行なうこと
を特徴とする精製水製造装置の殺菌方法。 In the sterilization treatment in the system of the purified water production apparatus that produces purified water from the raw water using each water treatment unit arranged sequentially between the raw water supply tank upstream and the purified water storage tank downstream,
While heating the purified water in the purified water storage tank, the solution is sent to the water treatment unit on the most upstream side, and the purified water is circulated in the purified water production apparatus.
When the temperature of the purified water in the uppermost stream water treatment unit reaches a predetermined temperature or more and is maintained for a predetermined time, the heating purified water feeding to the water treatment unit is stopped and the downstream side of the water treatment unit The heated water treatment unit located in the water treatment unit is started to feed heated purified water, circulates on the downstream side of the purified water production apparatus, and the same operation is performed on the downstream side water treatment unit. A method for sterilizing a purified water production apparatus.
少なくとも上流側から活性炭処理部、ナノ膜処理部および逆浸透膜処理部を有するものであって、
第１工程：加熱精製水を、前記活性炭処理部からナノ膜処理部および逆浸透膜処理部に順に循環させ、前記活性炭処理部の精製水の温度が、所定温度でかつ所定時間維持されたとき、前記活性炭処理部への送液を停止する工程。
第２工程：前記活性炭処理部への送液が停止されたのち、加熱精製水をナノ膜処理部から逆浸透膜処理部に循環させ、前記ナノ膜処理部の精製水の温度が、所定温度でかつ所定時間維持されたとき、前記ナノ膜処理部への送液を停止する工程。
第３工程：前記ナノ膜処理槽への送液が停止されたのち、加熱精製水を逆浸透膜処理部に循環させ、前記逆浸透膜処理部の精製水の温度が、所定温度でかつ所定時間維持されたとき、前記逆浸透膜処理槽への送液を停止する工程。
を順次実施すること
を特徴とする請求項４に記載の精製水製造装置の殺菌方法。 The purified water production apparatus is
It has at least an activated carbon treatment part, a nano membrane treatment part and a reverse osmosis membrane treatment part from the upstream side,
First step: When heated purified water is circulated in order from the activated carbon treatment unit to the nano membrane treatment unit and the reverse osmosis membrane treatment unit, and the temperature of the purified water in the activated carbon treatment unit is maintained at a predetermined temperature for a predetermined time. The process of stopping liquid feeding to the activated carbon treatment part.
Second step: After the liquid supply to the activated carbon treatment unit is stopped, the heated purified water is circulated from the nano membrane treatment unit to the reverse osmosis membrane treatment unit, and the temperature of the purified water in the nano membrane treatment unit is a predetermined temperature. And, when maintained for a predetermined time, stopping the liquid feeding to the nanofilm processing section.
Third step: After the liquid feeding to the nano membrane treatment tank is stopped, the heated purified water is circulated to the reverse osmosis membrane treatment unit, and the temperature of the purified water in the reverse osmosis membrane treatment unit is a predetermined temperature and a predetermined value. A step of stopping liquid feeding to the reverse osmosis membrane treatment tank when the time is maintained.
5. The method for sterilizing a purified water production apparatus according to claim 4, wherein the steps are sequentially performed.
処理部内温度を、少なくとも温度８０℃以上に保持することにより行なうこと
を特徴とする請求項４又は５に記載の精製水製造装置の殺菌方法。 The sterilization of each processing unit is
The method for sterilizing a purified water production apparatus according to claim 4 or 5, wherein the temperature in the processing section is maintained at least at a temperature of 80 ° C or higher.
１〜６０分であること
を特徴とする請求項６に記載の精製水製造装置の殺菌方法。 The holding time is
It is 1 to 60 minutes, The sterilization method of the purified water manufacturing apparatus of Claim 6 characterized by the above-mentioned.
常温状態の精製水の加熱開始と同時に、又は加熱によって精製水の温度を、所定温度に昇温中に開始させること
を特徴とする請求項４に記載の精製水製造装置の殺菌方法。 The purified water circulation is
5. The method for sterilizing a purified water production apparatus according to claim 4, wherein the temperature of the purified water is started at the same time as the heating of the purified water in the normal temperature state or during the temperature rise by heating.
を特徴とする請求項４又は５に記載の精製水製造装置の殺菌方法。 The sterilization with heated purified water is performed, and the raw material water is used to cool each of the heated processing units, and the raw material water used for cooling is discharged outside the system. The method for sterilizing a purified water production apparatus according to 4 or 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008160366A JP5093679B2 (en) | 2008-06-19 | 2008-06-19 | Disinfection method for purified water production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008160366A JP5093679B2 (en) | 2008-06-19 | 2008-06-19 | Disinfection method for purified water production equipment |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JP2010000433A true JP2010000433A (en) | 2010-01-07 |
| JP2010000433A5 JP2010000433A5 (en) | 2011-09-08 |
| JP5093679B2 JP5093679B2 (en) | 2012-12-12 |
Family
ID=41582584
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2008160366A Active JP5093679B2 (en) | 2008-06-19 | 2008-06-19 | Disinfection method for purified water production equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP5093679B2 (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011105566A1 (en) * | 2010-02-26 | 2011-09-01 | 株式会社日立製作所 | Seawater desalting system |
| JP2012055811A (en) * | 2010-09-07 | 2012-03-22 | Sharp Corp | Drinking water container provided with filter medium, and washing method of the filter medium |
| CN102976505A (en) * | 2012-10-31 | 2013-03-20 | 艾欧史密斯（上海）水处理产品有限公司 | Reverse osmosis water purifier |
| JP2013095504A (en) * | 2011-11-04 | 2013-05-20 | Nihon Pure Water Inc | Drinking water producing and filling system |
| JP2014091068A (en) * | 2012-11-01 | 2014-05-19 | Daicen Membrane Systems Ltd | Manufacturing apparatus of refined water for medical treatment, and operational method thereof |
| JP2014113512A (en) * | 2012-12-06 | 2014-06-26 | Daicen Membrane Systems Ltd | Apparatus for producing medical purified water and operation method of the same |
| JP2014128767A (en) * | 2012-12-28 | 2014-07-10 | Kurita Water Ind Ltd | Pure water production system |
| JP2017136541A (en) * | 2016-02-03 | 2017-08-10 | 三菱ケミカルアクア・ソリューションズ株式会社 | Medicinal purified water production apparatus and production method |
| CN112047556A (en) * | 2020-09-28 | 2020-12-08 | 开能康德威健康科技(北京)有限责任公司 | Water treatment facilities and hemodialysis system |
| JP2021003677A (en) * | 2019-06-26 | 2021-01-14 | 日本ウォーターシステム株式会社 | Water treatment apparatus |
| CN117582824A (en) * | 2023-11-28 | 2024-02-23 | 武汉启诚生物技术有限公司 | Water purification equipment heat sterilization method and water purification equipment heat sterilization system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004275881A (en) * | 2003-03-14 | 2004-10-07 | Kurita Water Ind Ltd | Ultrapure water manufacturing system |
| JP2007054784A (en) * | 2005-08-26 | 2007-03-08 | Nippon Rensui Co Ltd | Drainage treatment apparatus, rinser drainage recovery system and method for sterilizing drainage treatment apparatus |
| JP2009028602A (en) * | 2007-07-25 | 2009-02-12 | Mitsubishi Rayon Eng Co Ltd | Medical purified water manufacturing device and hot water disinfection method for nanofiltratioin membrane |
-
2008
- 2008-06-19 JP JP2008160366A patent/JP5093679B2/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004275881A (en) * | 2003-03-14 | 2004-10-07 | Kurita Water Ind Ltd | Ultrapure water manufacturing system |
| JP2007054784A (en) * | 2005-08-26 | 2007-03-08 | Nippon Rensui Co Ltd | Drainage treatment apparatus, rinser drainage recovery system and method for sterilizing drainage treatment apparatus |
| JP2009028602A (en) * | 2007-07-25 | 2009-02-12 | Mitsubishi Rayon Eng Co Ltd | Medical purified water manufacturing device and hot water disinfection method for nanofiltratioin membrane |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011105566A1 (en) * | 2010-02-26 | 2011-09-01 | 株式会社日立製作所 | Seawater desalting system |
| JP2011177601A (en) * | 2010-02-26 | 2011-09-15 | Hitachi Ltd | Seawater desalination system |
| JP2012055811A (en) * | 2010-09-07 | 2012-03-22 | Sharp Corp | Drinking water container provided with filter medium, and washing method of the filter medium |
| JP2013095504A (en) * | 2011-11-04 | 2013-05-20 | Nihon Pure Water Inc | Drinking water producing and filling system |
| CN102976505A (en) * | 2012-10-31 | 2013-03-20 | 艾欧史密斯（上海）水处理产品有限公司 | Reverse osmosis water purifier |
| JP2014091068A (en) * | 2012-11-01 | 2014-05-19 | Daicen Membrane Systems Ltd | Manufacturing apparatus of refined water for medical treatment, and operational method thereof |
| JP2014113512A (en) * | 2012-12-06 | 2014-06-26 | Daicen Membrane Systems Ltd | Apparatus for producing medical purified water and operation method of the same |
| JP2014128767A (en) * | 2012-12-28 | 2014-07-10 | Kurita Water Ind Ltd | Pure water production system |
| JP2017136541A (en) * | 2016-02-03 | 2017-08-10 | 三菱ケミカルアクア・ソリューションズ株式会社 | Medicinal purified water production apparatus and production method |
| JP2021003677A (en) * | 2019-06-26 | 2021-01-14 | 日本ウォーターシステム株式会社 | Water treatment apparatus |
| CN112047556A (en) * | 2020-09-28 | 2020-12-08 | 开能康德威健康科技(北京)有限责任公司 | Water treatment facilities and hemodialysis system |
| CN117582824A (en) * | 2023-11-28 | 2024-02-23 | 武汉启诚生物技术有限公司 | Water purification equipment heat sterilization method and water purification equipment heat sterilization system |
Also Published As
| Publication number | Publication date |
|---|---|
| JP5093679B2 (en) | 2012-12-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5093679B2 (en) | Disinfection method for purified water production equipment | |
| JP2010000433A5 (en) | ||
| JP3570304B2 (en) | Sterilization method of deionized water production apparatus and method of producing deionized water | |
| JP5923027B2 (en) | Apparatus for producing purified water for medical use and operation method thereof | |
| JP4949658B2 (en) | Dialysis water production apparatus and sterilization method thereof | |
| JP6036265B2 (en) | Apparatus and method for producing purified water for pharmaceutical production | |
| JP2004074109A (en) | Method and apparatus for manufacturing purified water for medicines | |
| JP6725143B2 (en) | Water treatment equipment | |
| JP2009028602A (en) | Medical purified water manufacturing device and hot water disinfection method for nanofiltratioin membrane | |
| JP2011147880A (en) | Method and apparatus for production of purified water for medicine | |
| JP2007237062A (en) | Artificial dialysis water manufacturing method and its manufacturing apparatus | |
| JP5336926B2 (en) | Purified water production method and purified water production apparatus | |
| JP2000189963A (en) | Fresh water making and production of fresh water | |
| JP5923030B2 (en) | Apparatus for producing purified water for medical use and operation method thereof | |
| JP5459704B2 (en) | Purified water production method and purified water production apparatus | |
| JP2021178297A (en) | Pharmaceutical water production system and its sterilization method | |
| JP5184401B2 (en) | Pure water production method and pure water production apparatus | |
| JP5903428B2 (en) | Disinfection method for electrodeionization equipment | |
| JP2011125863A (en) | Method for disinfecting nanofiltration membrane by hot water | |
| JP4617696B2 (en) | Sterilization method for pure water production apparatus and pure water production apparatus | |
| JP6956223B2 (en) | Purified water supply system and its operation method | |
| JP4712540B2 (en) | Pure water production apparatus and hot water sterilization method for pure water production apparatus | |
| JP6637320B2 (en) | Pharmaceutical purified water production apparatus and method for sterilizing pharmaceutical purified water production apparatus | |
| JP2013184105A (en) | Purified water manufacturing apparatus and method for drug manufacturing | |
| JP2020203231A (en) | Membrane penetration water production apparatus and injection service water production system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20110616 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20110616 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20120127 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20120313 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20120427 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20120821 |
|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20120906 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 5093679 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20150928 Year of fee payment: 3 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |