JPH11128957A - Improvement of quality of city water - Google Patents

Improvement of quality of city water

Info

Publication number
JPH11128957A
JPH11128957A JP33625297A JP33625297A JPH11128957A JP H11128957 A JPH11128957 A JP H11128957A JP 33625297 A JP33625297 A JP 33625297A JP 33625297 A JP33625297 A JP 33625297A JP H11128957 A JPH11128957 A JP H11128957A
Authority
JP
Japan
Prior art keywords
water
aqueous solution
pipe
slaked lime
tap
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.)
Pending
Application number
JP33625297A
Other languages
Japanese (ja)
Inventor
Mikio Omori
幹雄 大森
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.)
EIDAI KAIHATSU KK
Original Assignee
EIDAI KAIHATSU KK
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 EIDAI KAIHATSU KK filed Critical EIDAI KAIHATSU KK
Priority to JP33625297A priority Critical patent/JPH11128957A/en
Publication of JPH11128957A publication Critical patent/JPH11128957A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To downsize an apparatus having at least a specified number of water receiving tanks by producing a nearly saturated hydrated lime aqueous solution in a hydrated lime dissolving tank and a carbonic acid aqueous solution having a prescribed free carbonic acid concentration by a free carbonic acid concentration adjustment device and supplying these solutions to the tanks. SOLUTION: A nearly saturated hydrated lime aqueous solution W2 is produced in a hydrated lime dissolving tank 1 and supplied to two water receiving tanks 7a, 7b through an aqueous solution supply pipe 6. A carbonic acid aqueous solution W4 having a prescribed free carbonic acid concentration is produced by a free carbonic acid concentration adjustment device 11 and supplied to the tanks 7a, 7b through a carbonic acid aqueous solution supply pipe 18. Quality-improved water W6 is produced from the solutions w2 , w4 and city water W as raw water in the tanks 7a, 7b. In this process, since quality- improved water W6 can be produced by the use of one hydrated lime dissolving tank 1 and one free carbonic acid concentration adjustment device 11 and two water receiving tanks 7a, 7b, an apparatus can be downsized.

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】本発明は水道水改質装置、よ
り詳しくは、水道水に消石灰略飽和水溶液を注入してそ
の水道水を改質するようにした水道水改質装置に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a tap water reforming apparatus, and more particularly to a tap water reforming apparatus in which a substantially saturated aqueous solution of slaked lime is injected into tap water to reform the tap water. .

【0002】[0002]

【従来の技術】従来、既存のビルや高層住宅等において
は、水道用の配管内が腐食し、赤水が発生し、しばしば
問題となっているが、この対策として荷性ソーダ注入
法、ソーダ灰注入法、ライニング法や消石灰注入法等が
知られている。この内消石灰注入法は、単に赤水を防止
するだけでなくランゲリア指数(水の腐食性の判定指
標)の改善力が大きいことや主成分のカルシウムが健康
上に良いと言われていることなどにより近来多く実施さ
れている。この消石灰注入法は、攪拌機を有する消石灰
溶解槽内に消石灰を投入するとともに水道水の一部を供
給して攪拌し、消石灰をこの水道水に溶解して、消石灰
略飽和水溶液を製造し、一方遊離炭酸濃度調整装置に、
他の一部の水道水と炭酸ガスとを注入して所定の遊離炭
酸濃度を有する炭酸水となし、この炭酸水と前記した消
石灰略飽和水溶液と原水である水道水とを所定の比率で
受水槽に供給してこの水道水の水質を改善するものであ
る。即ち、水道水を改質処理し、ランゲリア指数を改善
するとともに消石灰が水道水中の炭酸ガス、具体的には
遊離炭酸と反応して炭酸カルシウムが生成し、これによ
り水道水中のカルシウム分が増加するとともにこの炭酸
カルシウムが水道管の内壁に付着して被膜を形成し、こ
の被膜により赤水の発生を防止するようにしたものであ
る。ところで、かかる消石灰注入法においては、原水で
ある水道水に消石灰略飽和水溶液を注入して、所定のP
H値以下(水道局規制によるPH値8.6以下)でかつ
ランゲリア指数が零に近い水道水に改質するためには、
水道水に含まれる遊離炭酸の濃度管理が重要である。そ
のため原水である水道水中の遊離炭酸濃度を計測し、炭
酸ガスの注入量を制御して予め水道水中の遊離炭酸濃度
を所定値となした後、受水槽に供給することが知られて
いる(例えば特開平2−194893号)。そして、こ
の受水槽に供給される水道水の供給量に対応した消石灰
略飽和水溶液が受水槽内に供給されるのである。このよ
うにして受水槽内で改善(改質)された水道水は送水ポ
ンプで使用場所、例えば集合住宅等へ供給されることと
なる。
2. Description of the Related Art Conventionally, in existing buildings and high-rise houses, the inside of water supply pipes is corroded and red water is generated, which is often a problem. An injection method, a lining method, a slaked lime injection method, and the like are known. This method of slaked lime injection not only prevents red water, but also has a great power to improve the Langeria index (index for determining the corrosiveness of water) and that calcium as the main component is said to be good for health. Many have been implemented recently. In this slaked lime injection method, slaked lime is charged into a slaked lime dissolving tank having a stirrer and a part of tap water is supplied and stirred, slaked lime is dissolved in the tap water to produce a slaked lime substantially saturated aqueous solution. For the free carbon dioxide concentration controller,
Another part of tap water and carbon dioxide gas are injected to form carbonated water having a predetermined free carbonic acid concentration, and the carbonated water, the above-described substantially slaked lime aqueous solution, and tap water as raw water are received at a predetermined ratio. The water is supplied to a water tank to improve the quality of the tap water. That is, the tap water is reformed to improve the Langeria index and slaked lime reacts with carbon dioxide in the tap water, specifically, free carbon dioxide to generate calcium carbonate, thereby increasing the calcium content in the tap water. At the same time, the calcium carbonate adheres to the inner wall of the water pipe to form a film, and this film prevents the generation of red water. In this slaked lime injection method, a substantially saturated aqueous solution of slaked lime is injected into tap water, which is raw water, and a predetermined P
In order to reform tap water whose H value is less than or equal to the PH value (8.6 or less according to the regulations of the Waterworks Bureau) and the Langeria index is close to zero,
It is important to control the concentration of free carbonic acid contained in tap water. Therefore, it is known that the concentration of free carbonic acid in tap water as raw water is measured, the amount of carbonic acid gas injected is controlled, the free carbonic acid concentration in tap water is set to a predetermined value, and then supplied to a receiving tank ( For example, JP-A-2-194893). Then, an approximately saturated aqueous solution of slaked lime corresponding to the supply amount of tap water supplied to the water receiving tank is supplied into the water receiving tank. The tap water that has been improved (reformed) in the water receiving tank in this way is supplied to a place of use, for example, an apartment house by a water pump.

【0003】[0003]

【発明が解決しようとする課題】ところで、従来、通常
の既存の集合住宅においては、水道水を一旦受水槽に貯
えた後、送水ポンプにより高架水槽に又は各住宅に送水
されているが、この受水槽は、清掃時の断水を防止する
ため複数(通常は2槽)設けられている。かかる複数の
受水槽を有する集合住宅において、前記したような水道
水改質装置を採用しようとすれば、各受水槽毎に消石灰
溶解槽や遊離炭酸濃度調整装置を設ける必要がある。そ
のため装置全体が大型となり広い据付面積が必要となる
ばかりでなく製作費も高くなり、かつ運転管理費も高く
なるという問題がある。
By the way, conventionally, in a conventional existing apartment house, tap water is temporarily stored in a receiving tank and then sent to an elevated water tank or each house by a water pump. A plurality of (usually two) water receiving tanks are provided to prevent water interruption during cleaning. In order to adopt the above-described tap water reforming apparatus in an apartment house having a plurality of water receiving tanks, it is necessary to provide a slaked lime dissolving tank and a free carbon dioxide concentration adjusting apparatus for each of the water receiving tanks. Therefore, there is a problem that not only the entire device becomes large and a large installation area is required, but also the production cost is increased and the operation management cost is also increased.

【0004】[0004]

【課題を解決するための手段】本発明は、前記したよう
な従来の問題点を解決するためになされたものであっ
て、一部の水道水と消石灰とを混合して消石灰略飽和水
溶液を製造する消石灰溶解槽と、一部の水道水に炭酸ガ
スを注入して所定の遊離炭酸濃度を有する炭酸水となす
遊離炭酸濃度調整装置と、前記消石灰略飽和水溶液と前
記炭酸水と原水である水道水とを混合して改質水となす
少なくとも2以上の受水槽とよりなり、前記消石灰溶解
槽と前記各受水槽とを夫々に水溶液注入装置を有する異
なる水溶液供給管により接続するとともに、前記遊離炭
酸濃度調整装置と前記各受水槽とを夫々に制御弁を有す
る異なる炭酸水供給管を接続し、かつ各受水槽に夫々原
水である水道水の給水管を接続するようにした水道水改
質装置を提供せんとするものである。かかる構成による
水道水改質装置によれば一つの消石灰溶解槽及び遊離炭
酸濃度調整装置により、製造された消石灰略飽和水溶液
と炭酸水とは夫々異なる水溶液供給管及び炭酸水供給管
を経て複数の受水槽に供給することができ、装置の小型
化を図ることができる。そして好ましくは、夫々の受水
槽には液面計が設けられこの液面計の信号により各受水
槽内に供給される原水である水道水と、消石灰略飽和水
溶液と炭酸水の供給量が所定の比率となるよう制御され
る。より具体的には、各受水槽には夫々上位液面計と下
位液面計とが設けられ、この各受水槽で製造された改質
水を使用場所へ送水すると、この液面が低下して来る。
そしてその液面が下位液面に達すると下位液面計から信
号を発し、原水である水道水の供給管に設けられた弁体
及び水溶液供給管に配置された水溶液注入装置、炭酸水
供給管に配置された制御弁を作動させて消石灰略飽和水
溶液と炭酸水と原水である水道水とを所定の比率でこの
受水槽内に供給して、ここで改質水を製造する。そし
て、この受水槽内の液面が上昇して上位液面に達すると
上位液面計からの信号により前記水溶液注入装置を停止
させるとともに前記制御弁と弁体を閉鎖するのである。
各受水槽が比較的近距離に配置されているときは、夫々
の受水槽には単位送水管の一端が接続され、この単位送
水管の他端は、送水装置を有する主送水管に接続され
る。そして主送水管であってかつ送水装置の上流側と受
水槽とはポンプ及びPH検知器を有する改質水の戻し管
で連結され、このポンプを作動させることにより主送水
管内の改質水のPHが検知される。このPH検知器の信
号は運転データとして収集されるが、この改質水のPH
が所定の範囲を外れたときは消石灰略飽和水溶液及び炭
酸水の供給を停止する。勿論、この改質水のPHが所定
の範囲を外れた場合、前記したように消石灰略飽和水溶
液及び炭酸水の供給を停止する方法に代えて、炭酸水供
給管に設けられた制御弁を制御するのが好ましい。即
ち、かかる水道水改質装置においては、消石灰と炭酸水
中に含まれる遊離炭酸とが中和反応して炭酸水素カルシ
ウムが生成され、水道水が改質されることとなるが、こ
の場合消石灰の供給量に対し遊離炭酸が少ないときは中
和反応が早期に完了し、ランゲリア指数の充分な改善が
なされない状態でPHが増大する。一方遊離炭酸が多過
ぎると、改質水中に腐蝕性の炭酸が残留するため好まし
くない。かかることから液面計からの信号(オン・オフ
信号)により、必要とする遊離炭酸を含有する炭酸水の
供給量より僅かに少ない供給量となるよう設定して置
き、そして受水槽で改質された改質水のPHをPH検知
器で計測し、その信号により炭酸水供給管に設けられた
制御弁を制御して、炭酸水の供給量を調整し、改質水の
PHが少なくとも水道法で定める所定の範囲(PH5.
8〜8.6)となるよう操作するのがよい。このような
構成によれば主送水管に配置された送水装置により各受
水槽内の改質水は単位送水管を経て同時に、又は必要に
応じて単位送水管に設けられた手動開閉弁を操作するこ
とにより、一方の受水槽内の改質水のみを使用場所に送
水することとなる。そのため各受水槽に夫々送水装置及
びPH検知器を有する送水管を設ける場合に較べて装置
を小型化かつ簡略化することができる。そして、この受
水槽が比較的大なる距離(例えば200m以上)を置い
て配置される場合には、消石灰溶解槽で製造された消石
灰略飽和水溶液は別の送液装置により中間槽に供給し、
ここで一旦貯えられ然る後水溶液注入装置を経て受水槽
に供給されるよう構成するのがよい。この場合各受水槽
には夫々送水装置を有する主送水管が接続されるととも
に、各受水槽には、夫々ポンプ及びPH検知器を有する
改質水の戻し管が設けられる。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned conventional problems, and comprises mixing a part of tap water and slaked lime to form a substantially saturated slaked lime aqueous solution. A slaked lime dissolving tank to be manufactured, a free carbon dioxide concentration adjusting device for injecting carbon dioxide gas into a part of tap water to form a carbonated water having a predetermined free carbon dioxide concentration, and the slaked lime substantially saturated aqueous solution, the carbonated water and raw water. It is composed of at least two or more water receiving tanks that are mixed with tap water to form reformed water, and the slaked lime dissolving tank and each of the water receiving tanks are connected by different aqueous solution supply pipes each having an aqueous solution injection device, A tap water reformer in which a different carbonated water supply pipe having a control valve is connected to each of the free carbon dioxide concentration adjusting device and each of the water receiving tanks, and a tap water supply pipe as raw water is connected to each of the water receiving tanks. Quality equipment Is shall. According to the tap water reforming apparatus having such a configuration, one slaked lime dissolving tank and a free carbon dioxide concentration adjusting device are used. It can be supplied to the water receiving tank, and the size of the device can be reduced. Preferably, a liquid level gauge is provided in each of the water receiving tanks, and the supply amounts of tap water, which is raw water supplied into each of the water receiving tanks in accordance with a signal from the liquid level gauge, and a substantially saturated aqueous solution of slaked lime and carbonated water are specified. Is controlled to be the ratio of More specifically, each receiving tank is provided with an upper level gauge and a lower level gauge, respectively, and when the reformed water produced in each of the receiving tanks is sent to the place of use, the level of the liquid drops. Come.
When the liquid level reaches the lower liquid level, a signal is issued from the lower liquid level gauge, and a valve element provided in the supply pipe of tap water as raw water, an aqueous solution injection device arranged in the aqueous solution supply pipe, a carbonated water supply pipe. By operating a control valve disposed in the water supply tank, a substantially saturated aqueous solution of slaked lime, carbonated water, and tap water as raw water are supplied at a predetermined ratio into the water receiving tank, and reformed water is produced here. Then, when the liquid level in the water receiving tank rises and reaches the upper liquid level, the signal from the upper liquid level meter stops the aqueous solution injector and closes the control valve and the valve body.
When each water tank is arranged at a relatively short distance, one end of a unit water pipe is connected to each water tank, and the other end of the unit water pipe is connected to a main water pipe having a water feeding device. You. The main water supply pipe and the upstream side of the water supply device and the water receiving tank are connected by a return pipe of the reformed water having a pump and a PH detector. By operating the pump, the reformed water in the main water supply pipe is operated. PH is detected. The signal of the PH detector is collected as operation data.
When the value is out of the predetermined range, the supply of the approximately saturated aqueous solution of slaked lime and the carbonated water is stopped. Of course, when the pH of the reformed water is out of the predetermined range, the control valve provided in the carbonated water supply pipe is controlled instead of the method of stopping the supply of the substantially slaked lime and the carbonated water as described above. Is preferred. That is, in such a tap water reforming apparatus, slaked lime and free carbonic acid contained in carbonated water undergo a neutralization reaction to generate calcium hydrogen carbonate, and the tap water is reformed. When the amount of free carbonic acid is small relative to the supplied amount, the neutralization reaction is completed early, and the PH increases without sufficient improvement of the Langeria index. On the other hand, if the amount of free carbonic acid is too large, corrosive carbonic acid remains in the reformed water, which is not preferable. Therefore, the signal (on / off signal) from the liquid level gauge is set so that the supplied amount of carbonated water containing free carbonic acid is slightly smaller than the required supply amount, and reformed in the receiving tank. The PH of the reformed water is measured by a PH detector, and a control valve provided in the carbonated water supply pipe is controlled by the signal to adjust the supply amount of the carbonated water. A prescribed range (PH5.
8 to 8.6). According to such a configuration, the reforming water in each of the water receiving tanks is simultaneously operated via the unit water supply pipe by the water supply device arranged in the main water supply pipe, or the manual open / close valve provided in the unit water supply pipe is operated as necessary. By doing so, only the reformed water in one of the water receiving tanks is sent to the place of use. Therefore, the size and the size of the apparatus can be reduced as compared with the case where a water supply apparatus and a water supply pipe having a PH detector are provided in each of the water receiving tanks. And when this water receiving tank is arranged at a relatively large distance (for example, 200 m or more), the slaked lime substantially saturated aqueous solution produced in the slaked lime dissolving tank is supplied to the intermediate tank by another liquid feeding device,
Here, it is preferable to be configured so as to be temporarily stored and then supplied to a water receiving tank via an aqueous solution injection device. In this case, a main water supply pipe having a water supply device is connected to each of the water receiving tanks, and a return pipe for reforming water having a pump and a PH detector is provided in each of the water receiving tanks.

【0005】[0005]

【実施例】以下図1及び図2に基づき本発明による水道
水改質装置の実施例を説明する。図1において、1は攪
拌機2を内装する消石灰溶解槽であってこの消石灰溶解
槽1には、消石灰aが投入されるとともに給水弁3を有
する第1の給水管4から一部の水道水Wが供給され、
ここで消石灰略飽和水溶液Wが製造される。給水弁3
は消石灰溶解槽1に設けられた液面計(図示せず)の信
号により操作されるようになっている。5は溶解残渣d
を排出する排出管である。この消石灰溶解槽1で製造さ
れた消石灰略飽和水溶液Wは、水溶液供給管6を経て
2つの受水槽7a,7bに供給されるようになってい
る。即ち、水溶液供給管6は主管6aと分岐管6bとよ
り構成され、この主管6aと分岐管6bには夫々水溶液
注入装置としての注入ポンプ8a,8bが設けられてい
る。この注入ポンプ8a,8bは可変容量型でもよいが
制御を簡略化するためには定量型が選択され、制御装置
10a,10bからの制御信号V〜Vにより操作さ
れるよう構成される。より詳しくは、受水槽7a,7b
に設けられた下位液面計9c,9dからの信号V5,V
6が制御装置10a,10bに入力されるとここで制御
信号V,Vが作成され、この制御信号V,V
より注入ポンプ8a,8bを作動させることにより消石
灰略飽和水溶液Wを受水槽7a,7bに供給する。そ
して液面WLが上位液面WLに達すると上位液面計9
a,9bからの信号V,Vが制御装置10a,10
bに入力されると制御信号V,Vが出力され、注入
ポンプ8a,8bを停止する。この実施例において水溶
液注入装置としての注入ポンプ8a,8bを有する異な
る水溶液供給管を主管6aと分岐管6bとにより構成し
たが、これらは必要に応じて主管6aを平列に配置して
もよい。一方、11は遊離炭酸濃度調整装置であって、
この遊離炭酸濃度調整装置11は、遊離炭酸濃度計12
と炭酸ガスボンベ13と混合槽14と制御弁15を有す
るガス管16と第2の供給管17とより構成されてい
る。そして一部の水道水Wが第2の供給管17から混
合槽14に供給されるとこの一部の水道水W中に含ま
れる遊離炭酸の量が遊離炭酸濃度計12により計測さ
れ、その信号Vが制御弁15に導かれ、この制御弁1
5を操作して炭酸ガスボンベ13内の炭酸ガスCをガス
管16を経て混合槽14内の水道水W中に注入し、所
定の遊離炭酸濃度を有する炭酸水Wが製造されるよう
になっている。この遊離炭酸濃度調整装置11において
は炭酸ガスCを混合槽14内において水道水Wと混合
させるようにしたが、これに代えてラインミキサーを用
いて混合させることもできる。このようにして製造され
た炭酸水Wは、炭酸水供給管18を経て受水槽7a,
7bに供給される。具体的には、炭酸水供給管18は主
管18aと分岐管18bとにより構成され、この主管1
8aと分岐管18bとには夫々制御弁19a,19bが
設けられ、この制御弁19a,19bは、前記注入ポン
プ8a,8bと同様に制御装置10からの制御信号V
〜Vにより制御されるようになっている。この場合に
おいても制御弁19a,19bを有する異なる炭酸水供
給管18を主管18aと分岐管18bとより構成した
が、これに代えて主管18aを平列に配置してもよい。
このようにして消石灰略飽和水溶液Wと炭酸水W
が供給される受水槽7a,7bにはFM弁の如き弁体2
0a,20bを有する第3の給水管21a,21bが接
続され、この弁体20a,20bも制御装置10a,1
0bからの制御信号V〜Vにより制御されるように
なっている。そしてこの弁体20a,20bを開放する
ことによりこの第3の給水管21a,21bから原水で
ある水道水Wが受水槽7a,7b内に供給されるよう
になっている。このようにして消石灰略飽和水溶液W
と炭酸水Wと原水である水道水Wとにより改質水W
が製造される。22a,22bは夫々手動による開閉
弁23a,23bを有する単位送水管であって、この単
位送水管22a,22bの一端は夫々受水槽7a,7b
に接続され、その他端は送水装置としての送水ポンプ2
5を有する主送水管26に接続されている。28は改質
水Wの戻し管であって、この戻し管28は一端が主送
水管26であってかつ送水ポンプ25の上流側に接続さ
れるとともに、その他端は、受水槽7aに接続されてい
る。そしてこの戻し管28にはポンプ29とPH検知器
30とが配置されている。31は改質水W6の使用場所
である集合住宅である。受水槽7a,7b内において製
造された改質水Wの一部はポンプ29により主送水管
26内から戻し管28を経て受水槽7aに戻されるがこ
のときPH検知器30からの信号V10が制御装置10
a,10bに入力され、ここで運転データとして収集さ
れるとともに記憶装置に予め入力されている所定の範囲
のPH値と比較され、この改質水WのPH値が所定の
PH値を外れた場合は必要により警報を発するととも
に、信号V,Vが出力され少なくとも注入ポンプ8
a,8b及び制御弁19a,19bを操作して受水槽消
石灰略飽和水溶液W及び炭酸水Wの供給を停止す
る。そして好ましくは、このPH検知器30の信号V
10を制御装置10a,10bに入力し所定のPHを得
るための炭酸水の供給量を求めて比例信号である制御信
号を別途作成し、この制御信号V11,V,12により
制御弁19a,19bを制御することにより、連続して
好適な改質水W6を製造することができる。そして改質
水Wは送水ポンプ25を作動させることにより単位送
水管22a,22b及び主送水管26を経て使用場所で
ある集合住宅31に送水することができる。このように
して受水槽7a,7b内の改質水Wを集合住宅31へ
送水すると液面WLが低下する。そしてこの液面WLが
下位液面WLに達すると下位液面計9c,9dからの
信号V,Vが発せられ、前述したようにこの信号V
,Vに基づく制御信号V,Vにより水溶液供給
管6である主管6a,分岐管6bに設けられた注入ポン
プ8a,8bが、また炭酸水供給管17である主管17
a,分岐管17bに設けられた制御弁18a,18b
が、更にまた第3の給水管21a,21bに設けられた
弁体20a,20bが操作され消石灰略飽和水溶液
,炭酸水W及び原水である水道水Wを所定の比
率でもって受水槽7a,7b内に供給して改質水W
製造する。そして受水槽7a,7bの液面WLが上位液
面WLに達すると上位液面計9a,9bから信号
,Vが発せられ、注入ポンプ8a,8bを停止す
るとともに制御弁19a,19b及び弁体20a,20
bを閉鎖する。勿論この場合、PH検知器30からの信
号V10により制御信号V〜Vを作成し、この制御
信号V〜Vを比例信号となし消石灰略飽和水溶液W
、炭酸水W、及び水道水Wの供給量を制御するこ
とも考えられるが制御系が複雑となるため、この信号V
〜Vをオン・オフ信号となし、予め設定された水道
水Wの時間当りの供給量を基に注入ポンプ8a,8b
による消石灰略飽和水溶液W及び制御弁19a,19
bによる炭酸水Wの供給量を定めておくのがよい。こ
の場合炭酸水Wの供給量は実験により求められた所定
の供給量より僅か少ない供給量となるよう設定しておく
のがよい。そして不測の事態、例えば水道水Wの供給
量が少ないか又は消石灰略飽和水溶液の供給量が多くな
ったときは改質水WのPHが所定値を超えることとな
る。このような場合前記したように消石灰略飽和水溶液
及び炭酸水の供給を停止するか又は必要によりこの改質
水WのPHが所定置を超えた場合にのみ制御信号V
11,V12を作成し、この制御信号V11,V12
比例信号として制御弁19a,19bを制御してより多
くの炭酸水Wを受水槽7a,7bに供給して改質水W
のPH値を低下させるのである。なお、各受水槽7
a,7bの何れか一方を清掃する場合は、開閉弁23a
又は23bを手動操作して閉鎖し清掃する受水槽7a又
は7b内の改質水Wの送水を停止することとなる。こ
の実施例において制御装置10a,10bを2基設けた
場合について示したがもちろん、この制御装置10a,
10bは1基としてもよい。図2は、本発明による水道
水改質装置の他の実施例を示す系統図であって、図1と
同一符号は同一名称を示す。この実施例は受水槽7aと
受水槽7bの距離Lが比較的遠く(例えば200m以
上)離れている場合に好適なものであって、消石灰溶解
槽1及び遊離炭酸濃度調整装置11は一方の受水槽7a
近傍に配置される。そして特に消石灰溶解槽1で製造さ
れた消石灰略飽和水溶液Wは、注入ポンプ8aにより
水溶液供給管6を構成する主管6aを介して受水槽7a
に、また送液装置である遠心ポンプ32を作動させ水溶
液供給管6を構成する分岐管6bにより他の受水槽7b
の近傍に配置された中間槽33に供給され、ここで一旦
貯えられた後注入ポンプ8bによりこの受水槽7bに供
給されるようになっている。そして、遠心ポンプ32は
中間槽33に設けられた例えばボールタップ式液面計の
信号により作動されるよう構成されている。この場合各
受水槽7a,7bには夫々PH検知器30a,30b及
びポンプ29a,29bとを有する戻し管28a,28
bが接続され、各受水槽7a,7b内の改質水WのP
Hが検知されるようになっている。そして、この送水ポ
ンプ25a,25bを作動させることにより各受水槽7
a,7b内の改質水Wを集合住宅31a,31bに供
給することができるようになっている。この実施例にお
いて遊離炭酸濃度調整装置11により製造された炭酸水
も受水槽7b近傍に中間槽を設け、この中間槽から
受水槽7b内に供給してもよいが、本来炭酸水Wは通
常の水道水と同一圧力を有するものであり、特に中間槽
は必要としない。前記実施例において弁体20a,20
bを各受水槽7a,7bに設けられた上位液面計9a,
9b及び下位液面計9c,9dからの信号V〜V
基づく信号V〜Vにより制御するようにしたが、こ
の弁体20a,20bをFM弁とすれば、この信号V
〜Vによる制御は必要としないことは明らかである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a tap water reforming apparatus according to the present invention will be described below with reference to FIGS. In FIG. 1, reference numeral 1 denotes a slaked lime dissolving tank in which a stirrer 2 is installed. Slaked lime a is charged into the slaked lime dissolving tank 1 and a part of tap water W is supplied from a first water supply pipe 4 having a water supply valve 3. 1 is supplied,
Here slaked substantially saturated aqueous solution W 2 is produced. Water valve 3
Is operated by a signal from a liquid level gauge (not shown) provided in the slaked lime dissolving tank 1. 5 is the melting residue d
It is a discharge pipe for discharging. The slaked lime dissolving vessel slaked lime substantially saturated aqueous solution W 2 produced by 1, two water tank 7a through the solution feed pipe 6, are supplied to 7b. That is, the aqueous solution supply pipe 6 includes a main pipe 6a and a branch pipe 6b, and the main pipe 6a and the branch pipe 6b are provided with injection pumps 8a and 8b as an aqueous solution injection apparatus, respectively. The infusion pump 8a, 8b is metered is selected in order to simplify the control may be a variable displacement type, the control device 10a, configured to be operated by the control signal V 1 ~V 4 from 10b. More specifically, the water receiving tanks 7a and 7b
V5, V5 from lower level gauges 9c, 9d provided in
6 the control unit 10a, is input to the 10b where control signal V 1, V 2 is created, slaked lime substantially saturated aqueous solution W 2 by operating the infusion pump 8a, 8b by the control signal V 1, V 2 Is supplied to the water receiving tanks 7a and 7b. The upper level gauge 9 when the liquid surface WL reaches the upper liquid surface WL 2
a, signal V 7, V 8 from 9b the control device 10a, 10
b, the control signals V 3 and V 4 are output, and the infusion pumps 8a and 8b are stopped. In this embodiment, different aqueous solution supply pipes having injection pumps 8a and 8b as an aqueous solution injection device are constituted by the main pipe 6a and the branch pipe 6b, but these may be arranged in parallel as required. . On the other hand, 11 is a free carbon dioxide concentration adjusting device,
The free carbonic acid concentration adjusting device 11 includes a free carbonic acid
And a gas pipe 16 having a control tank 15 and a second supply pipe 17. And the amount of free carbonic acid in which a part of the tap water W 3 included in the mixing tank when 14 is supplied into the tap water W 3 of the portion from the second supply pipe 17 is measured by the free carbon dioxide concentration meter 12, the signal V 9 is guided to the control valve 15, the control valve 1
5 is operated to inject the carbon dioxide gas C in the carbon dioxide gas cylinder 13 into the tap water W 3 in the mixing tank 14 via the gas pipe 16 so that the carbonated water W 4 having a predetermined free carbon dioxide concentration is produced. Has become. Although in this free carbon dioxide concentration adjusting device 11 has to be mixed with tap water W 3 carbon dioxide C in the mixing tank 14 may be mixed using a line mixer instead. Thus carbonated water W 4 that is manufactured, the water tank 7a through carbonated water supply pipe 18,
7b. Specifically, the carbonated water supply pipe 18 includes a main pipe 18a and a branch pipe 18b.
8a and the branch pipe 18b and the respective control valves 19a, 19b are provided, the control valve 19a, 19b, the control signal V 1 of the from the controller 10 the infusion pump 8a, like the 8b
It is controlled by ~V 4. Also in this case, the different carbonated water supply pipes 18 having the control valves 19a and 19b are constituted by the main pipe 18a and the branch pipe 18b, but the main pipes 18a may be arranged in parallel instead.
In this way slaked substantially saturated aqueous solution W 2 and receiving tank 7a where the carbonated water W 4 is supplied, the 7b such as FM valve the valve body 2
The third water supply pipes 21a and 21b each having the first and second valve bodies 20a and 20b are connected to the control devices 10a and 1b.
And it is controlled by a control signal V 1 ~V 4 from 0b. The valve body 20a, by opening 20b the third water supply pipe 21a, the tap water W 5 which is a raw water from 21b are supplied to the receiving tank 7a, a 7b. Thus, slaked lime almost saturated aqueous solution W 2
Reforming water W by the tap water W 5, which is a carbonated water W 4 and the raw water and
6 is manufactured. Reference numerals 22a and 22b denote unit water pipes having manually opened and closed valves 23a and 23b, respectively. One ends of the unit water pipes 22a and 22b are respectively connected to water tanks 7a and 7b.
The other end is a water pump 2 as a water supply device
5 is connected to a main water supply pipe 26 having the same. 28 is a return tube of the reforming water W 6, together with the return pipe 28 has one end connected to the upstream side of a by and water pump 25 primarily water pipe 26 and the other end connected to a water tank 7a Have been. The return pipe 28 is provided with a pump 29 and a PH detector 30. Reference numeral 31 denotes an apartment house where the reformed water W6 is used. Receiving tank 7a, but returned to the water tank 7a through the return pipe 28 from the main water supply pipe within 26 by the pump 29 is part of the reforming water W 6 produced within 7b signal V from PH detector 30 at this time 10 is the control device 10
a, it is inputted to 10b, where it is compared with the PH value of the predetermined range which is previously input to the storage device while being collected as operational data, PH value of the reforming water W 6 is out of a predetermined PH value In this case, an alarm is issued if necessary, and signals V 2 and V 4 are output and at least the infusion pump 8
a, 8b and the control valve 19a, by manipulating the 19b to stop supplying the water receiving tank slaked substantially saturated aqueous solution W 2 and carbonated water W 4. And preferably, the signal V of the PH detector 30
The control signal 10 is input to the control devices 10a and 10b to obtain a supply amount of carbonated water for obtaining a predetermined PH, a control signal as a proportional signal is separately created, and the control valves 19a and 19b are controlled by the control signals V 11 , V and 12 . by controlling the 19b, it is possible to produce a suitable reforming water W 6 consecutively. The reforming water W 6 being capable of water in collective housing 31 is a point of use through the unit water lines 22a, 22b and the main water pipe 26 by operating the water pump 25. Thus water receiving tank 7a, when the reforming water W 6 in 7b to water to collective housing 31 the liquid level WL is lowered. When this liquid surface WL reaches the lower liquid level WL 1 lower level gauge 9c, signal V 5, V 6 from 9d is emitted, the signal V as described above
5 and control signals V 1 and V 2 based on V 6 , the injection pumps 8 a and 8 b provided on the main pipe 6 a as the aqueous solution supply pipe 6 and the branch pipe 6 b, and the main pipe 17 as the carbonated water supply pipe 17.
a, control valves 18a, 18b provided in branch pipe 17b
Receiving but has furthermore a third water supply pipe 21a, the valve element 20a provided in 21b, 20b is operated slaked substantially saturated aqueous solution W 2, the tap water W 5 which is a carbonated water W 4 and the raw water at a predetermined ratio aquarium 7a, is supplied into 7b produces a reformed water W 6. The water tank 7a, the liquid level WL of 7b reaches the upper liquid surface WL 2 Top Level gauge 9a, signal V 7, V 8 is emitted from 9b, infusion pumps 8a, stops the 8b control valve 19a, 19b and valve bodies 20a, 20
b is closed. Of course in this case, to create a control signal V 1 ~V 4 the signal V 10 from PH detector 30, the control signal V 1 ~V 4 a proportional signal and without lime substantially saturated aqueous solution W
It is conceivable to control the supply amounts of 2 , carbonated water W 4 , and tap water W 5. However, since the control system becomes complicated, this signal V
1 ~V 4 on-off signals and without injection based on the feed rate per hour of the pre-set tap water W 5 pumps 8a, 8b
Aqueous lime substantially due to saturation W 2 and the control valve 19a, 19
good idea to set the supply amount of carbonated water W 4 by b. The supply amount of this carbonated water W 4 is better to previously set to be slightly smaller supply amount than the predetermined feed amount determined by experiments. The PH of the reforming water W 6 is to exceed the predetermined value when the contingency, for example, the supply amount of tap water W 5 supply amount is small, or hydrated lime substantially saturated aqueous solution of was increased. Only the control signal V when the or necessary to stop the supply of slaked lime substantially saturated aqueous solution and carbonated water as described above such case PH of the reforming water W 6 exceeds Tokoro stationary
11, to create a V 12, the control signal V 11, V 12 a control valve 19a as a proportional signal, receiving tank 7a more carbonated water W 4 by controlling the 19b, is supplied to 7b reforming water W
It lowers the PH value of 6 . In addition, each water receiving tank 7
a or 7b, the on-off valve 23a
Or 23b closed by manually operating the so that the stop water supply of the reforming water W 6 of the water receiving tank 7a or in 7b to clean. In this embodiment, the case where two control devices 10a and 10b are provided is shown, but of course, the control devices 10a and 10b
10b may be one group. FIG. 2 is a system diagram showing another embodiment of the tap water reforming apparatus according to the present invention, and the same reference numerals as those in FIG. 1 denote the same names. This embodiment is suitable when the distance L between the water receiving tank 7a and the water receiving tank 7b is relatively long (for example, 200 m or more), and the slaked lime dissolving tank 1 and the free carbon dioxide concentration adjusting device 11 are connected to one of the receiving tanks. Water tank 7a
It is arranged near. The water tank 7a particular slaked substantially saturated aqueous solution W 2 produced by slaked lime dissolving vessel 1, through the main pipe 6a constituting the aqueous solution feed pipe 6 by means of an infusion pump 8a
In addition, the centrifugal pump 32 which is a liquid feeding device is operated, and another water receiving tank 7b is formed by the branch pipe 6b constituting the aqueous solution supply pipe 6.
Is supplied to an intermediate tank 33 arranged near the tank, and once stored therein, is supplied to the water receiving tank 7b by an injection pump 8b. The centrifugal pump 32 is configured to be operated by a signal from, for example, a ball tap type liquid level meter provided in the intermediate tank 33. In this case, return pipes 28a, 28 having PH detectors 30a, 30b and pumps 29a, 29b are respectively provided in the water receiving tanks 7a, 7b.
b connected, each receiving tank 7a, P of the reforming water W 6 in 7b
H is detected. By operating the water pumps 25a and 25b, each of the water receiving tanks 7 is operated.
a, Housing 31a reforming water W 6 in 7b, so that the can be supplied to 31b. Carbonated water W 4 produced by free carbon dioxide concentration adjusting device 11 in this embodiment also an intermediate tank is provided in water receiving tank 7b vicinity may be supplied from the intermediate tank receiving tank within 7b but, naturally carbonated water W 4 Has the same pressure as ordinary tap water, and does not particularly require an intermediate tank. In the above embodiment, the valve bodies 20a, 20
b is the upper level gauge 9a provided in each of the water receiving tanks 7a, 7b,
9b and the lower level gauge 9c, was to be controlled by the signal V 1 ~V 4 based on the signal V 5 ~V 8 from 9d, the valve body 20a, if the 20b and FM valve, the signal V 1
Control by ~V 4 it is clear that not required.

【0006】[0006]

【発明の効果】以上の説明から明らかなように本発明に
よる水道水改質装置によれば、一つの消石灰溶解槽及び
遊離炭酸濃度調整装置により消石灰略飽和水溶液と所定
の遊離炭酸濃度を有する炭酸水とを製造し、この消石灰
略飽和水溶液と炭酸水とを2以上の受水槽に供給して水
道水の改質を行なうようにしたため、特に複数の受水槽
を有する既存の集合住宅等においては、小型の装置でも
って所定の水質を改善することができる。その結果装置
の据付面積の縮少化とともに装置の製作費や運転経費を
も削減することができるという大きな利点がある。
As is apparent from the above description, according to the tap water reforming apparatus according to the present invention, one slaked lime dissolving tank and a free carbon dioxide concentration adjusting device are used to mix a substantially saturated aqueous slaked lime aqueous solution with a carbonate having a predetermined free carbon dioxide concentration. Since water is produced and the substantially saturated aqueous solution of slaked lime and carbonated water are supplied to two or more water receiving tanks to reform tap water, especially in existing apartment houses having a plurality of water receiving tanks, etc. The predetermined water quality can be improved with a small device. As a result, there is a great advantage that the installation area of the apparatus can be reduced and the manufacturing cost and operation cost of the apparatus can be reduced.

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

【図1】本発明による水道水改質装置の一実施例を示す
系統図である。
FIG. 1 is a system diagram showing an embodiment of a tap water reforming apparatus according to the present invention.

【図2】本発明による水道水改質装置の他の実施例を示
す系統図である。
FIG. 2 is a system diagram showing another embodiment of the tap water reforming apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 消石灰溶解槽 4 第1の給
水管 2 攪拌機 5 排出管 3 給水弁 6 水溶液供
給管 7a,7b 受水槽 18 炭酸水供
給管 8a,8b 注入ポンプ 20a,20b
弁体 9a,9b 上位液面計 21a,21b
第3の給水管 9c,9d 下位液面計 22a,22b
単位送水管 10 制御装置 23a,23b
開閉弁 11 遊離炭酸濃度調整装置 25 送水ポン
プ 12 遊離炭酸濃度計 26 主送水管 13 炭酸ガスボンベ 28 戻し管 14 混合槽 29 ポンプ 16 ガス管 32 遠心ポン
プ 17 第2の給水管 33 中間槽
DESCRIPTION OF SYMBOLS 1 Slaked lime dissolution tank 4 First water supply pipe 2 Stirrer 5 Discharge pipe 3 Water supply valve 6 Aqueous solution supply pipe 7a, 7b Water receiving tank 18 Carbonated water supply pipe 8a, 8b Injection pump 20a, 20b
Valve body 9a, 9b Upper level gauge 21a, 21b
Third water pipe 9c, 9d Lower level gauge 22a, 22b
Unit water pipe 10 Control device 23a, 23b
Open / close valve 11 Free carbon dioxide concentration controller 25 Water pump 12 Free carbon dioxide meter 26 Main water pipe 13 Carbon dioxide gas cylinder 28 Return pipe 14 Mixing tank 29 Pump Reference Signs List 16 gas pipe 32 centrifugal pump 17 second water supply pipe 33 intermediate tank

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 一部の水道水と消石灰とを混合して消石
灰略飽和水溶液を製造する消石灰溶解槽と、一部の水道
水に炭酸ガスを注入して所定の遊離炭酸濃度を有する炭
酸水となす遊離炭酸濃度調整装置と、前記消石灰略飽和
水溶液と前記炭酸水と原水である水道水とを混合して改
質水となす少なくとも2以上の受水槽とよりなり、前記
消石灰溶解槽と前記各受水槽とを夫々に水溶液注入装置
を有する異なる水溶液供給管により接続するとともに、
前記遊離炭酸濃度調整装置と前記各受水槽とを夫々制御
弁を有する異なる炭酸水供給管により接続しかつ各受水
槽に原水である水道水の給水管を接続したことを特徴と
する水道水改質装置。
1. A slaked lime dissolving tank for producing an almost saturated aqueous solution of slaked lime by mixing a part of tap water and slaked lime, and a carbonated water having a predetermined free carbonic acid concentration by injecting carbon dioxide into a part of the tap water A free carbonic acid concentration adjusting device, and at least two or more water receiving tanks for mixing the carbonated water and tap water as raw water to form a reformed water by mixing the slaked lime substantially saturated aqueous solution with the tap water as raw water. Each of the receiving tanks is connected with a different aqueous solution supply pipe having an aqueous solution injection device, and
A tap water reforming device, wherein the free carbon dioxide concentration adjusting device and each of the receiving tanks are connected by different carbonated water supply pipes each having a control valve, and a tap water supply pipe as raw water is connected to each of the receiving tanks. Quality equipment.
【請求項2】 夫々の受水槽に液面計を設け、該液面計
の信号により各受水槽に供給される原水である水道水、
消石灰略飽和水溶液及び炭酸水の供給量を制御するよう
構成してなる請求項1記載の水道水改質装置。
2. A water level gauge is provided in each water receiving tank, and tap water which is raw water supplied to each water receiving tank by a signal of the liquid level gauge;
2. The tap water reforming apparatus according to claim 1, wherein a supply amount of the substantially saturated aqueous solution of slaked lime and the carbonated water is controlled.
【請求項3】 夫々の受水槽に夫々単位送水管の一端を
接続し、該各単位送水管の他端を送水装置を有する主送
水管に接続するよう構成してなる請求項1記載の水道水
改質装置。
3. The water supply according to claim 1, wherein one end of each unit water pipe is connected to each water receiving tank, and the other end of each unit water pipe is connected to a main water pipe having a water supply device. Water reformer.
【請求項4】 夫々の受水槽に送水装置を有する主送水
管を接続してなる請求項1記載の水道水改質装置。
4. The tap water reforming apparatus according to claim 1, wherein a main water supply pipe having a water supply device is connected to each of the water receiving tanks.
【請求項5】 ポンプとPH検知器とを有する改質水の
戻し管の一端を主送水管であってかつ送水装置の上流側
に接続するとともに該戻し管の他端を受水槽に接続して
なる請求項3記載の水道水改質装置。
5. One end of a return pipe for reforming water having a pump and a PH detector is connected to the main water supply pipe and upstream of the water supply device, and the other end of the return pipe is connected to a water receiving tank. 4. The tap water reforming apparatus according to claim 3, wherein
JP33625297A 1997-10-31 1997-10-31 Improvement of quality of city water Pending JPH11128957A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33625297A JPH11128957A (en) 1997-10-31 1997-10-31 Improvement of quality of city water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33625297A JPH11128957A (en) 1997-10-31 1997-10-31 Improvement of quality of city water

Publications (1)

Publication Number Publication Date
JPH11128957A true JPH11128957A (en) 1999-05-18

Family

ID=18297212

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33625297A Pending JPH11128957A (en) 1997-10-31 1997-10-31 Improvement of quality of city water

Country Status (1)

Country Link
JP (1) JPH11128957A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006187738A (en) * 2005-01-07 2006-07-20 Miura Co Ltd Waste water treatment apparatus
KR101129233B1 (en) 2009-07-30 2012-03-26 신도이앤씨 (주) A water pipes corrosion prevention system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006187738A (en) * 2005-01-07 2006-07-20 Miura Co Ltd Waste water treatment apparatus
JP4577016B2 (en) * 2005-01-07 2010-11-10 三浦工業株式会社 Wastewater treatment equipment
KR101129233B1 (en) 2009-07-30 2012-03-26 신도이앤씨 (주) A water pipes corrosion prevention system

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