JPH05200390A - Improvement of city water and device therefor - Google Patents

Improvement of city water and device therefor

Info

Publication number
JPH05200390A
JPH05200390A JP1030192A JP1030192A JPH05200390A JP H05200390 A JPH05200390 A JP H05200390A JP 1030192 A JP1030192 A JP 1030192A JP 1030192 A JP1030192 A JP 1030192A JP H05200390 A JPH05200390 A JP H05200390A
Authority
JP
Japan
Prior art keywords
water
carbon dioxide
slaked lime
line mixer
aqueous solution
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
JP1030192A
Other languages
Japanese (ja)
Other versions
JP2533820B2 (en
Inventor
Isao Funahashi
勲 舟橋
Kiwamu Yamamoto
究 山本
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.)
Kureha Corp
Kureha Engineering Co Ltd
Original Assignee
Kureha Corp
Kureha Engineering Co Ltd
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 Kureha Corp, Kureha Engineering Co Ltd filed Critical Kureha Corp
Priority to JP4010301A priority Critical patent/JP2533820B2/en
Publication of JPH05200390A publication Critical patent/JPH05200390A/en
Application granted granted Critical
Publication of JP2533820B2 publication Critical patent/JP2533820B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To miniaturize equipment and to effectively utilize gaseous carbon dioxide by blowing gaseous carbon dioxide into a pipeline to a water feed part from the water receiving part of a regulation tank, mixing and dissolving gaseous carbon dioxide by a line mixer and thereafter interlocking aqueous solution of slaked lime with the water feed amount, injecting water by automatic proportional control and feeding water to the water feed part of the regulation tank. CONSTITUTION:A dangelier index (LI) regulation tank 1 is partitioned into a water receiving part and a water feed part by a partition device 4. City water is lifted from the water receiving part by a pump 12 and sent to water feed part through a pipeline 5. Line mixers 6, 6' are provided in the pipeline 5. A gaseous carbon dioxide blowing device 7 is fitted to the upstream side of the line mixer 6. An injector 9 of a slaked lime aqueous solution is fitted to the upstream side of the line mixer 6'. Water is passed through a pipeline 5 in the amount correspondent to the amount of water supplied to the L1 regulation tank 1 through a water feed pipe 3. Gaseous carbon dioxide is blown into the water so that free carbonic acid is regulated to prescribed concentration. An aqueous solution of slaked lime is injected from the injector 9 in automatic control in a amount proportional to the water amount and the concentration of free carbonic acid.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、水道水の改良方法およ
び装置に関する。詳しくはランゲリア指数が低く腐食性
の強い水に炭酸ガスおよび消石灰水溶液を注入してラン
ゲリア指数を改良する方法およびそのための装置に関す
る。
FIELD OF THE INVENTION The present invention relates to a method and apparatus for improving tap water. More specifically, it relates to a method for injecting carbon dioxide gas and slaked lime aqueous solution into water having a low Langerian index and high corrosiveness to improve the Langerian index, and an apparatus therefor.

【0002】[0002]

【従来の技術】従来、水道管の腐食による赤水の発生を
防止するため、水道水のpHを高くする方法として、苛
性ソーダ注入法、ソーダ灰注入法、消石灰注入法等が知
られている。しかし、赤水防止のためには、単に水道水
のpHを高くするだけでは充分でなく、水道水の腐食性
の指標として知られているランゲリア指数を改善するこ
とが重要であることが認識されてきている。
2. Description of the Related Art Heretofore, as a method for increasing the pH of tap water in order to prevent the generation of red water due to corrosion of a water pipe, a caustic soda injection method, a soda ash injection method, a slaked lime injection method and the like are known. However, in order to prevent red water, it has been recognized that simply raising the pH of tap water is not enough, and it is important to improve the Langerian index, which is known as an index of corrosiveness of tap water. ing.

【0003】ランゲリア指数[LI]とは、アメリカの
ランゲリア氏によって提案された、水の腐食性の判定指
数であり、次式によって表される。
The Langeria index [LI] is a judgment index of water corrosivity proposed by Mr. Langeria of the United States, and is represented by the following equation.

【0004】[0004]

【数1】 [Equation 1]

【0005】LIが+なら炭酸カルシウムが水中から析
出する状態、−なら水中へ溶解する状態、0なら析出と
溶解が同時に起っている状態であるとされている。通
常、LIを−1より大にすると、腐食防止に有効である
と云われている。
It is said that when LI is +, calcium carbonate is precipitated from water, when it is −, it is dissolved in water, and when it is 0, precipitation and dissolution occur simultaneously. It is generally said that a LI greater than -1 is effective in preventing corrosion.

【0006】処理すべき水道水(以下、「原水」と云
う)中の遊離炭酸濃度が充分高いときは、消石灰を注入
するだけで中和反応により炭酸水素カルシウムを生成
し、大きなpHの変動なしにLIを改善し得る。しか
し、原水の遊離炭酸濃度が小さいときは少量の消石灰の
注入によって炭酸水素カルシウムの生成は終了し、あと
はpHのみが上昇してLIの充分な改善がなされない。
このため原水に予め炭酸ガスを溶解させておき、消石灰
水溶液を注入する方法が提案されている。
When the concentration of free carbonic acid in the tap water to be treated (hereinafter referred to as "raw water") is sufficiently high, calcium hydrogen carbonate is produced by a neutralization reaction only by injecting slaked lime, and there is no large change in pH. Can improve LI. However, when the concentration of free carbonic acid in the raw water is low, the production of calcium hydrogencarbonate is terminated by the injection of a small amount of slaked lime, and only the pH is raised thereafter, and the LI is not sufficiently improved.
Therefore, a method has been proposed in which carbon dioxide gas is dissolved in raw water in advance and the slaked lime aqueous solution is injected.

【0007】[0007]

【発明が解決しようとする課題】しかし、原水のpHを
水質基準(日本の場合上水道水のpHは5.8 〜8.6 )以
上に高くすることなく、原水のLIを改善するために炭
酸ガスおよび消石灰を注入する際に、例えば特開平2-19
4893号公報で提案されているように、それぞれの溶解槽
を設けることは設置面積が大きくなり好ましくない。更
に炭酸ガスの溶解を前記公報に記載されているように、
貯槽内の水に炭酸ガスを吹き込む方法のみでは炭酸ガス
の利用効率が悪く好ましくない。
However, carbon dioxide and slaked lime are added to improve the LI of raw water without raising the pH of the raw water above the water quality standard (in the case of Japan, the pH of tap water is 5.8 to 8.6). When injecting, for example, Japanese Patent Laid-Open No. 2-19
As proposed in Japanese Patent No. 4893, it is not preferable to provide each of the melting tanks because the installation area becomes large. Further, as described in the above publication, the dissolution of carbon dioxide gas,
The method of blowing carbon dioxide gas into the water in the storage tank alone is not preferable because the utilization efficiency of carbon dioxide gas is poor.

【0008】既存の浄水場やビルなどの貯水設備でLI
の改善を図ろうとする場合、敷地上の問題があり、設備
は小型であることが望まれる。また炭酸ガスも有効に利
用できることが望まれる。
[0008] LI is used in existing water treatment facilities such as water purification plants and buildings.
However, there is a problem on the site and it is desirable that the equipment is small. It is also desired that carbon dioxide gas can be effectively used.

【0009】本発明は、水道水のLIを改良するに当っ
ての上述のような要望に応じた方法および装置を提案す
ることを課題とする。
It is an object of the present invention to propose a method and a device according to the above needs in improving the LI of tap water.

【0010】[0010]

【課題を解決するための手段】本発明による水道水の改
良方法は水道水に炭酸ガスおよび消石灰水溶液を注入し
て水道水のLIを改良する方法において、下部に流通孔
を有する仕切り装置で受水部と送水部に仕切られている
LI調整槽の受水部から送水部へ送水される水道水の管
路に処理すべき水のLIと所望LIとから決定される濃
度になる量の炭酸ガスを吹込み、管路に設けられたライ
ンミキサーにより混合溶解せしめた後、該ラインミキサ
ー出口水に消石灰水溶液を送水量に連動して自動比例制
御注水し、LI調整槽の送水部へ送水することを特徴と
する。
A method for improving tap water according to the present invention is a method for improving LI of tap water by injecting carbon dioxide gas and a slaked lime aqueous solution into tap water. An amount of carbonic acid having a concentration determined from the LI of the water to be treated and the desired LI in the pipeline of tap water that is sent from the receiving part of the LI adjustment tank that is partitioned into the water part and the water sending part to the water sending part After gas is blown and mixed and dissolved by a line mixer provided in the pipeline, an aqueous solution of slaked lime is automatically proportionally injected into the outlet water of the line mixer in accordance with the amount of water to be fed, and then fed to the water feeding section of the LI adjusting tank. It is characterized by

【0011】また、本発明による水道水の改良装置は下
部に流通孔を有する仕切り装置で受水部と送水部に仕切
られたLI指数調整槽の受水部から送水部に至る管路に
ラインミキサーを設け、ラインミキサーの給水側に炭酸
ガス吹込み装置、該ラインミキサーの出口水側に消石灰
水溶液を注入する比例制御注入装置を設けることを特徴
とする。
Further, the tap water improving device according to the present invention is a partition device having a circulation hole at the bottom, and a line extending from the water receiving part to the water sending part of the LI index adjusting tank partitioned into the water receiving part and the water sending part. A mixer is provided, a carbon dioxide gas blowing device is provided on the water supply side of the line mixer, and a proportional control injection device for injecting a slaked lime aqueous solution is provided on the outlet water side of the line mixer.

【0012】以下、本発明を図1および図2により詳し
く説明する。
The present invention will be described in detail below with reference to FIGS. 1 and 2.

【0013】図1は、本発明の実施の態様を示す1例で
あり、ラインミキサーを2個設けた場合である。図1に
おいて、1はLI調整槽であり、通常の浄水処理された
原水の受水槽で、ビルなどの地下受水槽(貯水槽)など
をLIの改良調整するための槽として兼ねさせる。尤も
本発明の実施のために配水池の手前に設けられることも
ある。従って、本発明の処理後の水の貯水槽2が別途設
けられる。
FIG. 1 is an example showing an embodiment of the present invention, in which two line mixers are provided. In FIG. 1, reference numeral 1 denotes an LI adjustment tank, which is a water receiving tank for ordinary raw water that has been treated for water purification, and serves as an underground water receiving tank (water storage tank) of a building or the like as a tank for improving and adjusting LI. However, it may be provided in front of the reservoir for implementing the present invention. Therefore, the treated water storage tank 2 of the present invention is separately provided.

【0014】貯水槽2の水位の変動に応じて間欠的また
は連続的にLI調整槽1から送水され、LI調整槽1も
また給水管3より給水され水位を略一定に保つ。LI調
整槽1は、下部に流通孔を有する仕切り装置4によって
受水部と送水部とに仕切られており、この受水部からポ
ンプ12等で揚水された水道水がLI調整槽の外部に設け
られたパイプ等の管路5を通って、LI調整槽の送水部
に送水される。この管路5に2個のラインミキサー6,
6′を設ける。第1のラインミキサー6の手前に炭酸ガ
ス吹き込み装置7を、第2のラインミキサー6′の手前
に消石灰水溶液注入装置9を取り付ける。
Water is supplied from the LI adjusting tank 1 intermittently or continuously according to the fluctuation of the water level in the water storage tank 2, and the LI adjusting tank 1 is also supplied with water from the water supply pipe 3 to keep the water level substantially constant. The LI adjusting tank 1 is divided into a water receiving section and a water sending section by a partitioning device 4 having a circulation hole in the lower part, and tap water pumped from this water receiving section by a pump 12 or the like to the outside of the LI adjusting tank. Water is supplied to the water supply unit of the LI adjustment tank through the pipe line 5 such as the provided pipe. This line 5 has two line mixers 6,
6'is provided. A carbon dioxide gas blowing device 7 is installed in front of the first line mixer 6, and a slaked lime aqueous solution injection device 9 is installed in front of the second line mixer 6 '.

【0015】なお、仕切り装置4は、単一槽で処理前の
水と処理後の水の混合を避けるためのものであり、また
仕切り装置に設ける流通孔は受水部と送水部とで水位が
異なることから生じる不都合を避けることにある。
The partitioning device 4 is for avoiding the mixing of the water before the treatment and the water after the treatment in a single tank, and the flow holes provided in the partitioning device are the water level at the water receiving part and the water sending part. Is to avoid the inconvenience caused by the difference.

【0016】LI調整槽1に給水管3より供給される水
量に応じた量の水を管路5に通し、この水に遊離炭酸が
所定濃度になるよう炭酸ガスを吹き込む。遊離炭酸の所
定濃度とは、原水のLIと所望LIから、実験的に決め
られる濃度である。
An amount of water corresponding to the amount of water supplied from the water supply pipe 3 to the LI adjusting tank 1 is passed through the pipe 5, and carbon dioxide gas is blown into this water so that the free carbon dioxide has a predetermined concentration. The predetermined concentration of free carbonic acid is a concentration experimentally determined from the LI of the raw water and the desired LI.

【0017】炭酸ガスの注入は、炭酸ガス源(例えば、
炭酸ガスボンベ)8より炭酸ガス吹き込み装置7で水の
流量に比例した量の炭酸ガスを吹き込む。炭酸ガスを圧
入された水は第1のラインミキサー6で加圧下に炭酸ガ
スを強制溶解し、所定濃度の遊離炭酸含有水とし、第2
のラインミキサー6′に送られる。第2のラインミキサ
ー6′の直前に設けた消石灰水溶液注入装置9より、流
れる水の量および遊離炭酸濃度に比例した量の消石灰水
溶液が自動制御のもとに注入され、第2のラインミキサ
ー6′内で遊離炭酸含有水と反応して所望LIの炭酸水
素カルシウム含有水が得られる。消石灰水溶液の注入
は、具体的には処理後の水のpHを指標にpH計信号と
連動させて行なうのが簡便である。
The carbon dioxide gas is injected by a carbon dioxide gas source (for example,
Carbon dioxide gas is blown from the carbon dioxide cylinder 8 by the carbon dioxide blowing device 7 in an amount proportional to the flow rate of water. The water into which the carbon dioxide gas has been pressed is forcibly dissolved under pressure in the first line mixer 6 to obtain free carbonic acid-containing water having a predetermined concentration.
Sent to the line mixer 6 '. From the slaked lime aqueous solution injection device 9 provided immediately before the second line mixer 6 ′, an amount of slaked lime aqueous solution proportional to the amount of flowing water and the free carbonic acid concentration is injected under automatic control, and the second line mixer 6 The reaction with free carbonic acid-containing water results in the desired LI of calcium hydrogencarbonate-containing water. Specifically, it is convenient to inject the slaked lime aqueous solution by linking the pH of the water after treatment with the pH meter signal.

【0018】なお、図1において10は消石灰水溶液製造
槽である。水道水の改善に用いる消石灰水溶液は、消石
灰の注入量を調整する上から略飽和水溶液として調整し
ておくのが好ましい。消石灰略飽和水溶液とは、約1600
ppm 濃度の消石灰水溶液を指す。このような消石灰水溶
液の調整は、例えば特公昭 63-2890号公報に記載されて
いるような装置、即ち数十時間から数百時間連続運転し
得る量の消石灰を予め充填した溶解槽の下部から水を供
給して低速で攪拌しながら槽上部から消石灰水溶液を連
続的に取り出す装置を用いて行なうことができる。
In FIG. 1, 10 is a slaked lime aqueous solution manufacturing tank. The slaked lime aqueous solution used to improve tap water is preferably prepared as a substantially saturated aqueous solution in order to adjust the injection amount of slaked lime. About 1600 slaked lime saturated aqueous solution
A slaked lime aqueous solution with a ppm concentration. Such adjustment of the slaked lime aqueous solution, for example, from a device as described in JP-B-63-2890, that is, from the bottom of the dissolution tank pre-filled with an amount of slaked lime that can be continuously operated for several tens to several hundred hours. It can be carried out using a device in which water is supplied and the aqueous slaked lime solution is continuously taken out from the upper part of the tank while stirring at low speed.

【0019】ラインミキサーとしては配管内に流体の接
触混合を良好に行わせるエレメント(多孔板、充填材
等)を内蔵したものが用いられ、管路の長さにより異な
るが一般に長さ20〜100cm のものが用いられる。
As the line mixer, one having a built-in element (perforated plate, filling material, etc.) for favorably performing contact mixing of fluids in the pipe is used, and generally the length is 20 to 100 cm although it varies depending on the length of the pipe line. What is used.

【0020】図1に示したように注入する炭酸ガスおよ
び消石灰はともにラインミキサーで強制混合するのが混
合及び反応が完全となるので好ましい。しかし、場合に
よっては、即ち使用水量に対し比較的大容量のLI調整
槽1を設置し得る場合には、図2に示すように消石灰水
溶液は注入筒11を通してLI調整槽1に直接注入しても
よい。なお、図中12は水中ポンプ、13はpH計を示す。
As shown in FIG. 1, the carbon dioxide gas and slaked lime to be injected are preferably both force-mixed by a line mixer because the mixing and reaction are completed. However, in some cases, that is, when the LI adjusting tank 1 having a relatively large capacity for the amount of water used can be installed, the slaked lime aqueous solution is directly injected into the LI adjusting tank 1 through the injection cylinder 11 as shown in FIG. Good. In the figure, 12 is a submersible pump and 13 is a pH meter.

【0021】以下、実施例をあげて本発明を具体的に説
明する。
The present invention will be specifically described below with reference to examples.

【0022】[0022]

【実施例】実施例1 処理する原水を分析したところ、カルシウム硬度21ppm
、総アルカリ度23ppm、遊離炭酸濃度7.2ppm、pH6.4
、LI−2.8 であった。
Example 1 When the raw water to be treated was analyzed, the calcium hardness was 21 ppm.
, Total alkalinity 23ppm, free carbon dioxide concentration 7.2ppm, pH 6.4
, LI-2.8.

【0023】この原水を非腐食性のLI+0.5 の水に改
善するべく予備的に、原水に炭酸ガスを溶解させて遊離
炭酸濃度が10〜40ppm の水を調整し、濃度約1600ppm 、
pH12.7の消石灰水溶液を添加してpHが8.0 〜8.6 に
おさまり、且つ、LIが+0.5 になる遊離炭酸濃度を実
験的に求めたところ、遊離炭酸濃度28.8ppm 、pH5.8
であった。LIを+0.5 としたときのpHは8.5 であっ
た。
In order to improve this raw water into non-corrosive LI + 0.5 water, carbon dioxide gas is dissolved in the raw water to prepare water having a free carbon dioxide concentration of 10 to 40 ppm, and the concentration is about 1600 ppm.
When the free carbonic acid concentration at which the pH was suppressed to 8.0 to 8.6 and LI was +0.5 by adding a slaked lime aqueous solution having a pH of 12.7 was experimentally determined, the free carbonic acid concentration was 28.8 ppm and the pH was 5.8.
Met. The pH was 8.5 when LI was +0.5.

【0024】図1に示すように装置を用いて原水のLI
の改善を行なった。
An LI of raw water was prepared using an apparatus as shown in FIG.
Has been improved.

【0025】0.4m3 の消石灰溶解槽に消石灰20kgを充
填し、槽下部より原水を供給し低速攪拌機により攪拌し
て濃度約1600ppm の消石灰水溶液(pH12.7)を生成さ
せた。
A 0.4 m 3 slaked lime dissolution tank was filled with 20 kg of slaked lime, raw water was supplied from the bottom of the tank and stirred by a low speed stirrer to generate an aqueous slaked lime solution (pH 12.7) having a concentration of about 1600 ppm.

【0026】一方、下部に流通孔のある仕切り装置によ
り受水部と送水部に仕切られたLI調整槽(容積6
3 )に原水を 12m3 /Hr で供給し、長さ50cmのライン
ミキサー2個を有する受水部から送水部に至る管路に 1
2m3 /Hr で揚水し、該管路の第1のラインミキサーの上
流の管内に炭酸ガスボンベより炭酸ガスを0.34kg/Hr で
吹込み、ラインミキサーにより水に混合吸収させ、pH
5.8 、遊離炭酸濃度28.8ppm の水とし、ついでこの遊離
炭酸含有水にpH12.7の消石灰水溶液を第2のラインミ
キサー出口水のpHが8.5 になるように注入しながら第
2のラインミキサーに供給しLI調整槽の送水部に戻
し、送水部に設置されている送水ポンプで貯水槽に送水
した。このようにしてpH6.4 、LI−2.8 の水から、
pH8.5 、LI+0.5 の水を連続的に貯水槽に送ること
ができた。
On the other hand, the LI adjusting tank (volume 6) is divided into a water receiving part and a water sending part by a partitioning device having a flow hole at the bottom.
The raw water is supplied to M 3 ) at 12 m 3 / Hr, and it has a line mixer with two 50 cm long line mixers.
Pump water at 2m 3 / Hr, blow carbon dioxide at 0.34kg / Hr from a carbon dioxide cylinder into the pipe upstream of the first line mixer in the pipeline, mix with water with a line mixer to absorb, and pH
5.8, water with a free carbon dioxide concentration of 28.8 ppm, and then supply to the second line mixer while pouring a slaked lime aqueous solution having a pH of 12.7 into the water containing the free carbon dioxide so that the pH of the outlet water of the second line mixer becomes 8.5. Then, the water was returned to the water supply section of the LI adjustment tank, and water was supplied to the water storage tank by the water supply pump installed in the water supply section. Thus, from water of pH 6.4 and LI-2.8,
Water of pH 8.5 and LI + 0.5 could be continuously sent to the water tank.

【0027】実施例2 処理する原水を分析したところ、カルシウム硬度21ppm
、総アルカリ度23ppm、遊離炭酸濃度7.2ppm、pH6.4
でLI−2.8 であった。
Example 2 The raw water to be treated was analyzed and found to have a calcium hardness of 21 ppm.
, Total alkalinity 23ppm, free carbon dioxide concentration 7.2ppm, pH 6.4
It was LI-2.8.

【0028】この原水を非腐食性のLI+0.3 の水に改
善するべく予備的に、原水に炭酸ガスを溶解させて遊離
炭酸濃度が10〜40ppm の水を調整し、濃度約1600ppm の
消石灰水溶液を添加してpHが8.0 〜8.6 におさまり、
且つ、LIが+0.3 になる遊離炭酸濃度を実験的に求め
たところ、遊離炭酸濃度17.2ppm であった。LI+0.3
としたときのpHは8.3 であった。
In order to improve this raw water into non-corrosive LI + 0.3 water, carbon dioxide gas is dissolved in the raw water to prepare water having a free carbonic acid concentration of 10 to 40 ppm, and a slaked lime aqueous solution having a concentration of about 1600 ppm is prepared. PH is adjusted to 8.0-8.6 by adding
Moreover, when the free carbonic acid concentration at which the LI became +0.3 was experimentally determined, the free carbonic acid concentration was 17.2 ppm. LI + 0.3
The pH was 8.3.

【0029】図2に示すような装置を用いて原水のLI
の改善を行なった。
An LI of raw water was prepared using an apparatus as shown in FIG.
Has been improved.

【0030】0.4m3 の消石灰溶解槽に消石灰20kgを充
填し、槽下部より原水を供給し低速攪拌機により攪拌し
て濃度約1600ppm の消石灰水溶液(pH12.7)を生成さ
せた。
A 0.4 m 3 slaked lime dissolution tank was filled with 20 kg of slaked lime, raw water was supplied from the bottom of the tank and stirred by a low speed stirrer to generate a slaked lime aqueous solution (pH 12.7) having a concentration of about 1600 ppm.

【0031】一方、下部に流通孔のある仕切り装置によ
り受水部と送水部に仕切られたLI調整槽(容積25
3 )に原水を12m3 /Hr で供給し、受水部から送水部
に至る管路に12m3 /Hr で揚水し、該管路に設けた長さ
1mのラインミキサー上流の管内に炭酸ガスボンベより
調整弁で圧力を2kg/ cm3 になるようにして炭酸ガスを
0.12kg/Hr で吹込み、ラインミキサーにより水に混合吸
収させ、pH6.2 の遊離炭酸含有水とし、LI調整槽の
送水部に戻した。これと同時にLI調整槽からの出口水
のpHが8.3 になるように消石灰溶解槽よりpH12.7の
消石灰水溶液を注入筒を通して直接注入した。この水の
LIは+0.3 であった。
On the other hand, a LI adjusting tank (volume 25
The raw water to M 3) was supplied at 12m 3 / Hr, pumped in the 12m 3 / Hr to the conduit leading to the water supply portion from the water receiving portion, carbonate line mixer upstream of tube length 1m provided in the conduit Adjust the pressure from the gas cylinder to 2 kg / cm 3 with a regulating valve and add carbon dioxide gas.
It was blown with 0.12 kg / Hr, mixed with water by a line mixer and absorbed to give free carbonic acid-containing water of pH 6.2, which was returned to the water feeding section of the LI adjusting tank. At the same time, a slaked lime aqueous solution having a pH of 12.7 was directly injected from the slaked lime dissolution tank so that the pH of the outlet water from the LI adjustment tank was 8.3. The LI of this water was +0.3.

【0032】[0032]

【発明の効果】本発明によれば水道水のLI改良のため
の炭酸ガスの溶解を特別な炭酸ガス溶解槽を用いること
なく管路内のラインミキサー内で行なわせることにより
装置はコンパクトになる。従って本発明によればビルの
地下受水槽のように既に貯水槽がある場合、これをLI
調整槽として利用し、新たな設置面積を殆ど要すること
なくLIの改良を行うことができる。更に消石灰水溶液
と遊離炭酸含有水との反応を第2のラインミキサーで行
なわせる場合はより炭酸水素カルシウムの生成が容易と
なり小容量のLI調整槽の場合に適する。
According to the present invention, the apparatus becomes compact by dissolving carbon dioxide gas for improving the LI of tap water in a line mixer in a pipeline without using a special carbon dioxide gas dissolving tank. .. Therefore, according to the present invention, if there is already a water storage tank such as the underground water storage tank of a building, this
The LI can be improved by using it as an adjusting tank and requiring almost no new installation area. Further, when the reaction between the slaked lime aqueous solution and the free carbonic acid-containing water is carried out in the second line mixer, the production of calcium hydrogen carbonate becomes easier, which is suitable for a small capacity LI adjusting tank.

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

【図1】本発明の水道水の改善方法の一つの実施態様を
示すフローシートである。
FIG. 1 is a flow sheet showing one embodiment of a method for improving tap water of the present invention.

【図2】本発明の水道水の改善方法の他の実施態様を示
すフローシートである。
FIG. 2 is a flow sheet showing another embodiment of the method for improving tap water of the present invention.

【符号の説明】[Explanation of symbols]

1 LI調整槽 2 貯水槽 3 給水管 4 仕切り装置 5 管路 6、6′ ラインミキサー 7 炭酸ガス吹き込み装置 8 炭酸ガス源 9 消石灰水溶液注入装置 10 消石灰水溶液製造槽 11 注入筒 12 水中ポンプ 13 pH計 1 LI adjustment tank 2 Water storage tank 3 Water supply pipe 4 Partition device 5 Pipe line 6, 6'line mixer 7 Carbon dioxide gas blowing device 8 Carbon dioxide gas source 9 Slaked lime aqueous solution injection device 10 Slaked lime aqueous solution manufacturing tank 11 Injection cylinder 12 Submersible pump 13 pH meter

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 水道水に炭酸ガスおよび消石灰水溶液を
注入して水道水のランゲリア指数を改良する方法におい
て、下部に流通孔を有する仕切り装置で受水部と送水部
に仕切られているランゲリア指数調整槽の受水部から送
水部へ送水される水道水の管路に処理すべき水のランゲ
リア指数と所望ランゲリア指数とから決定される濃度に
なる量の炭酸ガスを吹込み、管路に設けられたラインミ
キサーにより混合溶解せしめた後、該ラインミキサー出
口水に消石灰水溶液を送水量に連動して自動比例制御注
水し、ランゲリア指数調整槽の送水部へ送水することを
特徴とする水道水の改良方法。
1. A method for injecting carbon dioxide gas and a slaked lime aqueous solution into tap water to improve the Langeria index of tap water, which is divided into a water receiving part and a water sending part by a partitioning device having a through hole at the bottom. The pipe of tap water sent from the water receiving part to the water sending part of the adjusting tank is blown with carbon dioxide gas in an amount having a concentration determined from the Langerian index of the water to be treated and the desired Langerian index, and provided in the conduit. After being mixed and dissolved by the line mixer, the tap water is characterized in that the slaked lime aqueous solution is automatically and proportionally injected into the outlet water of the line mixer in accordance with the amount of water to be fed, and is fed to the water feeding section of the Langeria index adjusting tank. Improvement method.
【請求項2】 水道水に炭酸ガスおよび消石灰水溶液を
注入して水道水のランゲリア指数を改良する方法におい
て、下部に流通孔を有する仕切り装置で受水部と送水部
に仕切られているランゲリア指数調整槽の受水部から送
水部へ送水される水道水の管路に処理すべき水のランゲ
リア指数と所望ランゲリア指数とから決定される濃度に
なる量の炭酸ガスを吹込み、管路に設けられた第1のラ
インミキサーにより混合溶解せしめた後、該ラインミキ
サー出口水に消石灰水溶液を送水量に連動して自動比例
制御注水し、第2のラインミキサーで混合した後、ラン
ゲリア指数調整槽の送水部へ送水することを特徴とする
水道水の改良方法。
2. A method for improving the Langerian index of tap water by injecting carbon dioxide gas and slaked lime aqueous solution into tap water, the Langerian index being divided into a water receiving part and a water sending part by a partitioning device having a circulation hole in the lower part. The pipe of tap water sent from the water receiving part to the water sending part of the adjusting tank is blown with carbon dioxide gas in an amount having a concentration determined from the Langerian index of the water to be treated and the desired Langerian index, and provided in the conduit. After being mixed and dissolved by the first line mixer, the slaked lime aqueous solution is automatically proportionally injected into the outlet water of the line mixer in association with the amount of water to be fed, and the mixed water is mixed in the second line mixer, and then the Langeria index adjusting tank A method for improving tap water, which comprises supplying water to a water supply section.
【請求項3】 下部に流通孔を有する仕切り装置で受水
部と送水部に仕切られたランゲリア指数調整槽の受水部
から送水部に至る管路にラインミキサーを設け、ライン
ミキサーの給水側に炭酸ガス吹込み装置、該ラインミキ
サーの出口水側に消石灰水溶液を注入する比例制御注入
装置を設けることを特徴とする水道水の改良装置。
3. A line mixer is provided in a pipe line extending from the water receiving part to the water sending part of a Langerian index adjusting tank partitioned into a water receiving part and a water sending part by a partitioning device having a circulation hole at a lower part, and a water supply side of the line mixer. An apparatus for improving tap water, characterized in that a carbon dioxide gas blowing device and a proportional control injection device for injecting a slaked lime aqueous solution are provided on the outlet water side of the line mixer.
JP4010301A 1992-01-23 1992-01-23 Method and apparatus for improving tap water Expired - Fee Related JP2533820B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4010301A JP2533820B2 (en) 1992-01-23 1992-01-23 Method and apparatus for improving tap water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4010301A JP2533820B2 (en) 1992-01-23 1992-01-23 Method and apparatus for improving tap water

Publications (2)

Publication Number Publication Date
JPH05200390A true JPH05200390A (en) 1993-08-10
JP2533820B2 JP2533820B2 (en) 1996-09-11

Family

ID=11746439

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4010301A Expired - Fee Related JP2533820B2 (en) 1992-01-23 1992-01-23 Method and apparatus for improving tap water

Country Status (1)

Country Link
JP (1) JP2533820B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010137224A (en) * 2010-02-12 2010-06-24 Kureha Engineering Co Ltd Method for cleaning water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010137224A (en) * 2010-02-12 2010-06-24 Kureha Engineering Co Ltd Method for cleaning water

Also Published As

Publication number Publication date
JP2533820B2 (en) 1996-09-11

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