JPH09248568A - Production of purified water and purified water reduction device used therefore - Google Patents

Production of purified water and purified water reduction device used therefore

Info

Publication number
JPH09248568A
JPH09248568A JP6063296A JP6063296A JPH09248568A JP H09248568 A JPH09248568 A JP H09248568A JP 6063296 A JP6063296 A JP 6063296A JP 6063296 A JP6063296 A JP 6063296A JP H09248568 A JPH09248568 A JP H09248568A
Authority
JP
Japan
Prior art keywords
pure water
water
water tank
purified water
tank
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
Application number
JP6063296A
Other languages
Japanese (ja)
Other versions
JP3217958B2 (en
Inventor
Morohei Sakaguchi
諸平 阪口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP06063296A priority Critical patent/JP3217958B2/en
Publication of JPH09248568A publication Critical patent/JPH09248568A/en
Application granted granted Critical
Publication of JP3217958B2 publication Critical patent/JP3217958B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent deterioration of water quality of purified water when water level control for maintaining the purified water level in a purified water tank in a constant range is performed. SOLUTION: When raw water supplied from a raw water tank 1 is made into purified water with a water purifying tower 2 and the purified water is stored in the purified water tank 3 the purified water 18 produced with the water purifying tower 2 is circulate to the raw water tank 1 during a period that the water level of the purified water 18 stored in the purified water tank 3 reaches an upper limit, value and then the water level decreases to a prescribed value.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、純水の製造方法
およびそれに用いる純水製造装置に関するものであり、
とくに、純水塔に対する原水の供給量の変動、ひいて
は、それに起因する純水水質の低下を防止するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pure water producing method and a pure water producing apparatus used therefor,
In particular, it is intended to prevent fluctuations in the amount of raw water supplied to the pure water tower, and consequently to prevent deterioration of the quality of pure water.

【0002】[0002]

【従来の技術】たとえば、連続冷延鋼板の製造設備にお
ける純水洗浄工程では、純水を連続的に供給することが
必須となるも、純水製造装置の根幹をなす純水塔は、一
定量の純水の製造後に、陰陽それぞれのイオン交換樹脂
の再生のための処理を施すことが必要になるので、一の
純水塔によって純水を連続的に製造することは不可能で
ある。そこで従来は、原水槽に、相互に並列配置した二
本の純水塔を連結した純水製造装置において、いずれか
一方の純水塔に再生処理を施す場合に、他方の純水塔を
作用させる運転サイクルを採用し、純水の連続的な製造
を可能ならしめている。
2. Description of the Related Art For example, in a deionized water cleaning process in a continuous cold-rolled steel sheet manufacturing facility, it is essential to continuously supply deionized water, but the deionized water tower that forms the basis of the deionized water manufacturing apparatus has a fixed amount. Since it is necessary to perform a process for regenerating the ion-exchange resins for each of the Yin and Yang after the production of pure water, it is impossible to continuously produce pure water by one pure water tower. Therefore, conventionally, in a pure water production apparatus in which two pure water towers that are arranged in parallel to each other are connected to a raw water tank, when one of the pure water towers is subjected to regeneration treatment, the other pure water tower is operated in an operating cycle. Is adopted to enable continuous production of pure water.

【0003】[0003]

【発明が解決しようとする課題】ところで、このような
従来技術にあっては、使用する純水塔の切り換え時にも
なお、純水の連続的な送給を担保するために、製造され
た純水を一定量貯留するバッファタンク、すなわち、純
水槽の設置が必要となる。ここで、このような純水槽に
おいては、そこでの純水の水面レベルを一定範囲内に制
御することが不可避となるため、通常は、純水の使用量
よりも大きな純水製造能力を有する純水製造装置で製造
された純水の、純水槽への貯留量が所定値に達した場合
に装置の運転を停止し、一方、その貯留量が所定値まで
減少した場合に、装置の運転を再開することで水面レベ
ルの制御を行っていた。
By the way, in such a conventional technique, pure water produced in order to ensure continuous feed of pure water even when the pure water tower to be used is switched. It is necessary to install a buffer tank that stores a certain amount of water, that is, a pure water tank. Here, in such a deionized water tank, it is inevitable to control the water surface level of the deionized water within a certain range. Therefore, in general, a pure water tank having a pure water production capacity larger than the amount of pure water used is required. When the amount of pure water produced by the water production device stored in the pure water tank reaches a specified value, the operation of the device is stopped, while when the amount of stored water decreases to a specified value, the operation of the device is stopped. The water level was controlled by restarting.

【0004】しかしながら、このような水面レベル制御
によれば、純水塔に対する原水の供給をオンオフするこ
とに起因して、その純水塔内に混合収容した陰および陽
のそれぞれのイオン交換樹脂が比重差で分離し、これに
より、通水再開直後に製造される純水の水質が大きく低
下するという問題があった。そこで、かかる問題点を解
決すべく、純水塔の出側に、純水槽の水面レベルを一定
に維持する流量調整弁を設置し、そこからの純水の送出
量に応じた量の純水を純水槽に流入させる技術が提案さ
れているが、これによれば、高価な流量計測装置や調整
装置が必要になることに加え、純水洗浄工程の停止その
他によって純水送給量が急激に変動した場合には、流量
調整弁の開度も急激に変化するので、上記水面レベル制
御と同様の問題が生じて、純水の水質の低下を十分に防
止することができない不都合があった。
However, according to such a water level control, since the raw water supply to the pure water tower is turned on and off, the respective negative and positive ion exchange resins mixed and accommodated in the pure water tower have a difference in specific gravity. There was a problem that the water quality of the pure water produced immediately after the resumption of water flow was significantly reduced. Therefore, in order to solve such a problem, a flow rate adjusting valve that maintains a constant water surface level in the pure water tank is installed on the outlet side of the pure water tower, and pure water in an amount suitable for the amount of pure water delivered from that valve is installed. A technique has been proposed in which the deionized water is introduced into the deionized water tank. However, according to this technique, an expensive flow rate measuring device and an adjusting device are required, and the deionized water supply amount is rapidly increased by stopping the deionized water washing process. When it fluctuates, the opening degree of the flow rate control valve also changes rapidly, so that the same problem as in the water surface level control arises, and there is the inconvenience that the deterioration of the quality of pure water cannot be sufficiently prevented.

【0005】この発明は、従来技術の有するこのような
問題点を有利に解決するものであり、製造された純水の
流動経路の変更によって純水槽の水面レベルを制御する
ことで、高価な流量計測装置や調整装置を用いる必要な
しに、純水の水質を十分定常なものとすることができ、
また、純水送給量の急激な変動に対しても水質を高く維
持することができる純水の製造方法およびそれに用いる
純水製造装置を提供することにある。
The present invention advantageously solves the above-mentioned problems of the prior art. By controlling the water level of the pure water tank by changing the flow path of the pure water produced, the expensive flow rate can be controlled. The quality of pure water can be made sufficiently steady without the need to use a measuring device or adjusting device.
It is another object of the present invention to provide a pure water production method and a pure water production apparatus used for the same, which can maintain high water quality even with a rapid change in the pure water feed rate.

【0006】[0006]

【課題を解決するための手段】この発明の純水の製造方
法は、原水槽と、並列配置した複数本の純水塔と、純水
槽とを順次に配設してなる純水製造装置によって純水を
製造するに際し、純水槽に貯留される純水の水面レベル
が上限値に達した後、その水面レベルが所定値に低下す
るまでの間、純水塔で製造された純水を、前記原水槽に
環流させるものである。この方法では、純水槽の水面レ
ベルのいかんにかかわらず、原水槽の原水を純水塔に定
常的に供給して、純水塔への原水供給量の変動を防止す
ることで、純水の水質低下のおそれを有効に除去するこ
とができ、また、水面レベルの制御は、純水槽への貯留
量に応じて、定常的に製造される純水の一部もしくは全
部を原水槽へ環流させることで簡単に行うことができ
る。
A method for producing pure water according to the present invention is a pure water producing apparatus comprising a raw water tank, a plurality of deionized water towers arranged in parallel, and a pure water tank. In producing water, the pure water produced in the pure water tower is charged with the pure water produced in the pure water tower until the water surface level of the pure water stored in the pure water tank reaches the upper limit and the water surface level decreases to a predetermined value. It is to recirculate in a water tank. With this method, regardless of the water level of the pure water tank, the raw water in the raw water tank is constantly supplied to the pure water tower to prevent fluctuations in the amount of raw water supplied to the pure water tower, thus reducing the quality of pure water. In addition, the water level can be effectively controlled by circulating part or all of the pure water that is constantly produced to the raw water tank, depending on the storage amount in the pure water tank. Easy to do.

【0007】また、この発明の純水製造装置は、順次に
連結した原水槽と、相互に並列配置した複数本の純水塔
と、純水槽とを具える純水製造装置において、純水塔と
純水槽との間から、前記原水槽に開口する環流通路を分
岐させたものである。この装置では、環流通路を設ける
だけの簡単にして安価な構造をもって前記方法を実施す
ることができる。
Further, the pure water producing apparatus of the present invention is a pure water producing apparatus comprising a raw water tank connected in sequence, a plurality of pure water towers arranged in parallel with each other, and a pure water tank. A circulation passage opening to the raw water tank is branched from the water tank. With this device, the method can be carried out with a simple and inexpensive structure in which only a circulation passage is provided.

【0008】[0008]

【発明の実施の形態】以下に、この発明の実施の形態を
図面に基づいて説明する。図1は、発明装置の一の実施
態様を示す回路図であり、図中1は原水槽を、2は、相
互に並列配置した図では二本の純水塔のそれぞれを示
し、そして3は、各純水塔2で製造された純水を貯留す
る純水槽を示す。ここでは、原水槽1とそれぞれの純水
塔2とを、原水送給通路4により連結し、この原水送給
通路4の、原水槽近傍部分には原水ポンプ5を、そして
純水塔近傍部分には、それぞれの原水切換弁6をそれぞ
れ設ける。また、それぞれの純水塔2と純水槽3とを純
水通路7によって連結し、この純水通路7に、上流側か
ら順次に、それぞれの純水切換弁8および導電率計9を
設ける。さらに、純水槽3に、純水送出ポンプ10を設
けた純水送出通路11を接続し、この純水送出通路11
にて、純水槽3に一旦貯留された純水を、所要の洗浄設
備等に導く。なお、純水槽3の内側には水位検出装置1
2および紫外線殺菌装置13のそれぞれを配設する。こ
こで、この装置では、導電率計9より下流側の位置で、
純水通路7から分岐する環流通路14を設け、この環流
通路14の先端を原水槽1に開口させるとともに、環流
通路14の分岐基部に環流切換弁15を、そして、純水
通路7の、環流通路分岐位置より下流側部分に純水吐出
弁16をそれぞれ設ける。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a circuit diagram showing one embodiment of the invented apparatus, in which 1 is a raw water tank, 2 is each of two pure water towers in a diagram in which they are arranged in parallel with each other, and 3 is The pure water tank which stores the pure water manufactured by each pure water tower 2 is shown. Here, the raw water tank 1 and each of the pure water towers 2 are connected by a raw water feed passage 4, a raw water pump 5 is provided near the raw water tank, and a raw water pump 5 is provided near the pure water tower. , Each raw water switching valve 6 is provided. Further, the pure water tower 2 and the pure water tank 3 are connected by a pure water passage 7, and the pure water switching valve 8 and the conductivity meter 9 are sequentially provided in the pure water passage 7 from the upstream side. Further, a pure water delivery passage 11 provided with a pure water delivery pump 10 is connected to the pure water tank 3, and this pure water delivery passage 11 is connected.
At, the pure water once stored in the pure water tank 3 is guided to a required cleaning facility or the like. In addition, the water level detection device 1 is provided inside the pure water tank 3.
2 and the ultraviolet sterilizer 13 are provided. Here, in this device, at a position downstream of the conductivity meter 9,
A reflux passage 14 is provided to branch from the pure water passage 7, the tip of the reflux passage 14 is opened to the raw water tank 1, a reflux switching valve 15 is provided at the branch base of the reflux passage 14, and a reflux flow of the pure water passage 7 is controlled. Pure water discharge valves 16 are provided at the downstream side of the passage branching position.

【0009】以上のように構成してなる装置では、いず
れか一方の純水塔2の原水切換弁6および純水切換弁8
の開放下で、原水ポンプ5を作動させて原水槽内の原水
をその純水塔2に流下させることにより、原水は、そこ
に含まれる陰陽それぞれのイオンを、純水塔内に予め収
容した陰陽それぞれのイオン交換樹脂17に交換吸着さ
れて純水とされ、しかる後、導電率計9を経て純水槽3
に流下される。このようにして純水槽内に流下した純水
18は、そこに貯留されるとともに、紫外線殺菌装置1
3によって殺菌され、そして、洗浄設備等における所要
純水量に応じて、純水送出ポンプ10を経て送水され
る。
In the apparatus constructed as described above, the raw water switching valve 6 and the pure water switching valve 8 of either one of the pure water towers 2 are arranged.
The raw water in the raw water tank is made to flow down into the pure water tower 2 by operating the raw water pump 5 under the open condition of the raw water. Pure water is exchanged and adsorbed by the ion exchange resin 17 of FIG.
Be washed away. The pure water 18 that has flowed into the pure water tank in this manner is stored therein, and the ultraviolet sterilizer 1
3 is sterilized, and water is sent through the pure water delivery pump 10 according to the required amount of pure water in the cleaning equipment or the like.

【0010】ところで、上述のような純水製造過程にお
いて、純水槽内の純水量が増加して、その水面レベルが
上限値に達したことを水位検出装置12によって検知し
た場合には、純水の定常的な製造を継続しつつ、環流切
換弁15を開放し、純水吐出弁16を閉止することによ
り、製造された純水を、環流通路14を経て原水槽1に
環流させる。ここで、環流純水量は、製造された純水の
全てとすることはもちろん、それの一部とすることも可
能である。
In the pure water production process as described above, when the water level detecting device 12 detects that the amount of pure water in the pure water tank has increased and the water surface level has reached the upper limit value, the pure water is detected. By continuing the steady production of the above, the circulation switch valve 15 is opened and the pure water discharge valve 16 is closed, so that the produced pure water is circulated to the raw water tank 1 through the circulation passage 14. Here, the amount of the circulating pure water may be not only all of the manufactured pure water but also a part thereof.

【0011】この一方で、純水槽内の水面レベルが所定
値まで低下した場合には、純水の製造はそのままに、純
水吐出弁16の開放および環流切換弁15の閉止を行っ
て、純水18の、純水槽3への流下を再開させる。とこ
ろで、この場合もまた、純水の製造量と、純水槽内の水
面レベルの増加割合との関連において、製造された純水
の一部についての環流を継続させることも可能である。
On the other hand, when the water surface level in the pure water tank drops to a predetermined value, the pure water discharge valve 16 is opened and the return flow switching valve 15 is closed while the pure water is still produced. The flow of the water 18 into the pure water tank 3 is restarted. By the way, also in this case, it is possible to continue the circulation of a part of the produced pure water in relation to the production amount of the pure water and the increasing rate of the water surface level in the pure water tank.

【0012】このことによれば、原水ポンプ5による原
水の供給量および、純水塔2による純水の製造量に実質
的な変動をもたらすことなしに、純水槽3の水面レベル
を制御することができるので、製造される純水18の水
質の低下を、簡単な設備構造をもって極めて効果的に防
止することができる。
According to this, the water surface level of the pure water tank 3 can be controlled without causing substantial fluctuations in the amount of raw water supplied by the raw water pump 5 and the amount of pure water produced by the pure water tower 2. Therefore, the deterioration of the quality of the pure water 18 produced can be extremely effectively prevented with a simple equipment structure.

【0013】なお、このような水面レベル制御を行うに
際し、純水塔2を通過する流量の変動を極力抑制するた
めには、弁15,16のそれぞれを、二秒以上の時間を
かけて開閉作動させることが好ましく、また、環流切換
弁15の開放後、時間をおいて純水吐出弁16を閉止す
るとともに、純水吐出弁16の開放から時間をおいて環
流切換弁15を閉止するシーケンス制御を行うことが好
ましい。
In order to suppress fluctuations in the flow rate passing through the deionized water tower 2 as much as possible when performing such water surface level control, each of the valves 15 and 16 is opened and closed by taking a time of 2 seconds or more. It is preferable to perform the sequence control in which the pure water discharge valve 16 is closed after a certain period of time after opening the reflux switch valve 15 and the reflux switch valve 15 is closed after a period of time from the opening of the pure water discharge valve 16. Is preferably performed.

【0014】[0014]

【実施例】以上に述べたこの発明の水面レベル制御によ
る純水水質の変化を導電率計をもって測定したところ、
図2に実線をもって示す通りとなった。なお、図中の破
線は、原水ポンプの運転を停止および再開する従来の水
面レベル制御による水質変化を示す。図2に示すグラフ
によれば、この発明および従来技術のいずれにあって
も、純水槽への純水の再供給時の水質の低下は余儀なく
されるが、この発明によれば、導電率の最高値を定常時
の約3倍程度に抑えることができるのに対し、従来技術
では、導電率の最高値が約30倍程度にまで増加するこ
とがわかる。
EXAMPLE A change in the quality of pure water by the water surface level control of the present invention described above was measured with a conductivity meter.
As shown by the solid line in FIG. The broken line in the figure shows the water quality change due to the conventional water surface level control for stopping and restarting the operation of the raw water pump. According to the graph shown in FIG. 2, in both the present invention and the prior art, the quality of the water is inevitably deteriorated when the pure water is re-supplied to the pure water tank. It can be seen that the maximum value can be suppressed to about 3 times that in the steady state, whereas in the conventional technique, the maximum value of the conductivity is increased to about 30 times.

【0015】[0015]

【発明の効果】従って、この発明の方法によれば、水面
レベル制御に際する水質の低下を有効に防止することが
でき、また、この発明の装置によれば、環流通路14を
設けるだけの、簡単にして安価な構造をもって発明方法
を容易に実施することができる。
Therefore, according to the method of the present invention, it is possible to effectively prevent the deterioration of the water quality during the control of the water surface level, and according to the apparatus of the present invention, only the circulation passage 14 is provided. The invention method can be easily implemented with a simple and inexpensive structure.

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

【図1】発明装置の一の実施形態を示す回路図である。FIG. 1 is a circuit diagram showing an embodiment of an inventive device.

【図2】純水槽への純水の再供給時の導電率の変化を示
すグラフである。
FIG. 2 is a graph showing a change in conductivity when pure water is re-supplied to a pure water tank.

【符号の説明】[Explanation of symbols]

1 原水槽 2 純水塔 3 純水槽 4 原水送給通路 5 原水ポンプ 7 純水通路 8 純水切換弁 9 導電率計 10 純水送出ポンプ 11 純水送出通路 12 水位検出装置 14 環流通路 15 環流切換弁 16 純水吐出弁 17 イオン交換樹脂 18 純水 1 Raw water tank 2 Pure water tower 3 Pure water tank 4 Raw water feed passage 5 Raw water pump 7 Pure water passage 8 Pure water switching valve 9 Conductivity meter 10 Pure water delivery pump 11 Pure water delivery passage 12 Water level detector 14 Recirculation passage 15 Recirculation switching Valve 16 Pure water discharge valve 17 Ion exchange resin 18 Pure water

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 原水槽と、並列配置した複数本の純水塔
と、純水槽とを順次に配設してなる純水製造装置によっ
て純水を製造するに際し、 純水槽に貯留される純水の水面レベルが上限値に達した
後、その水面レベルが所定値に低下するまでの間、純水
塔で製造された純水を、前記原水槽に環流させることを
特徴とする純水の製造方法。
1. Pure water stored in a pure water tank when pure water is manufactured by a pure water manufacturing apparatus in which a raw water tank, a plurality of pure water towers arranged in parallel, and a pure water tank are sequentially arranged. The method for producing pure water, characterized in that, after the water surface level of the water reaches the upper limit value, the pure water produced in the pure water tower is refluxed to the raw water tank until the water surface level decreases to a predetermined value. .
【請求項2】 順次に連結した原水槽と、相互に並列配
置した複数本の純水塔と、純水槽とを具える純水製造装
置において、 純水塔と純水槽との間から、前記原水槽に開口する環流
通路を分岐させたことを特徴とする純水製造装置。
2. A pure water production apparatus comprising a raw water tank which is sequentially connected, a plurality of pure water towers arranged in parallel with each other, and a pure water tank, wherein the raw water tank is provided between the pure water tower and the pure water tank. A pure water producing device, characterized in that a circulation passage opening to the side is branched.
JP06063296A 1996-03-18 1996-03-18 Pure water production method Expired - Fee Related JP3217958B2 (en)

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JP3217958B2 JP3217958B2 (en) 2001-10-15

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005169365A (en) * 2003-12-05 2005-06-30 Catalysts & Chem Ind Co Ltd Fluidized bed circulation type ion exchange device
JP2010162543A (en) * 2010-03-19 2010-07-29 Asahi Soft Drinks Co Ltd Water treatment apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005169365A (en) * 2003-12-05 2005-06-30 Catalysts & Chem Ind Co Ltd Fluidized bed circulation type ion exchange device
JP2010162543A (en) * 2010-03-19 2010-07-29 Asahi Soft Drinks Co Ltd Water treatment apparatus

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