JPS6146293A - Method for converting freshwater into drinking water - Google Patents

Method for converting freshwater into drinking water

Info

Publication number
JPS6146293A
JPS6146293A JP16734784A JP16734784A JPS6146293A JP S6146293 A JPS6146293 A JP S6146293A JP 16734784 A JP16734784 A JP 16734784A JP 16734784 A JP16734784 A JP 16734784A JP S6146293 A JPS6146293 A JP S6146293A
Authority
JP
Japan
Prior art keywords
water
carbon dioxide
filter
freshwater
fresh water
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
JP16734784A
Other languages
Japanese (ja)
Other versions
JPH0361518B2 (en
Inventor
Naohiko Ugawa
直彦 鵜川
Hiroshi Ogawa
弘 小川
Tsumoru Nakamura
中村 積
Masahiro Matsubayashi
松林 正博
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP16734784A priority Critical patent/JPS6146293A/en
Publication of JPS6146293A publication Critical patent/JPS6146293A/en
Publication of JPH0361518B2 publication Critical patent/JPH0361518B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To convert easily freshwater into drinking water by measuring the resistivity value of the water after passing through a filter, and regulating the amt. of gaseous carbon dioxide to be blown into the freshwater when freshwater is made drinkable by passing the freshwater through the filter packet with limestone, etc. CONSTITUTION:Gaseous carbon dioxide-contg. gas generated from an apparatus is blown into freshwater, which is formed in the seawater desalination apparatus by evaporation, to obtain gaseous carbon dioxide-contg. water. Then the gaseous carbon dioxide-contg. water is passed through a filter, packed with granular materials of limestone and/or dolomite, to increase the hardness. The resistivity value of the water after passing through the filter is continuously detected, and the amt. of said gaseous carbon dioxide-contg. gas to be blown in is regulated so that the resistivity value may be regulated to a specified value.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、蒸発法による半水の淡水化装置で、生成した
淡水に硬度成分を添加して飲料水を得る方、法に関する
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for obtaining drinking water by adding a hardness component to fresh water produced in a half-water desalination apparatus using an evaporation method.

蒸発法海水淡水化装置で得られる淡水は蒸留水であるた
め各種のイオン及び溶存ガス類をは、とんと、含まず、
カルシウムやマグネシウムの硬度成分もほとんど無い。
Since the fresh water obtained by the evaporation method seawater desalination equipment is distilled water, it does not contain all kinds of ions and dissolved gases.
Hardness components such as calcium and magnesium are almost absent.

このため上記・淡水をその11汎用の送水設備を使用し
て送水した場合には、送水設備に使用されている鋼管の
腐食、コンクリート材・の溶出現象が起こり、送水設備
の機能を損う恐九がある。一方飲料水として使用した場
合には前述理由により無味であり飲料水としての飲み味
が悪いばかりでなく心臓病の原因となり得ることが指摘
されてい、る。
For this reason, if the fresh water mentioned above is conveyed using 11 general-purpose water conveyance equipment, corrosion of the steel pipes used in the water conveyance equipment and elution of concrete materials may occur, which may impair the function of the water conveyance equipment. There is nine. On the other hand, when used as drinking water, it has been pointed out that for the reasons mentioned above, it is tasteless and not only tastes bad, but can also cause heart disease.

〔従来の技術〕   、 このため従来、より例えば文献「Desalinati
on 。
[Prior Art] Therefore, in the past, for example, the document "Desalinati
On.

39(1981)503−520J K紹介されティる
ように硬度増加剤として生石灰、消石灰1石灰石、ドロ
マイト等が使用され、これらを淡水に溶解させる方法が
行なわれてきたが、このうち石灰石及び/又はドロマイ
トを用いる場合、これ等を粒状にして充填したフィルタ
ー(飲料水化装置では石灰石及び/又はドロマイトの充
填層を通常フィルターと呼称)にあらかじめ炭酸ガスを
吹き込んだ淡水を導き、カルシウムあるいはマグネシウ
ムを重炭酸塩として溶出させて水の硬度を増す方法が一
般的である。
39 (1981) 503-520 J K, quicklime, slaked lime, dolomite, etc. have been used as hardness increasing agents, and a method of dissolving these in fresh water has been carried out, but among these, limestone and/or When using dolomite, fresh water into which carbon dioxide gas has been blown is introduced into a filter filled with granules (in drinking water production equipment, a bed of limestone and/or dolomite is usually called a filter), and calcium or magnesium is added to the filter. A common method is to increase the hardness of water by eluting it as carbonate.

炭酸ガス源としては、別途燃料を燃焼させて得た排ガス
中の炭酸ガスを回収する方法、炭酸ガスボンベで搬入す
る方法等が提案されているが、中でも最近淡水化装置自
体から発生する炭酸ガスを有効利用する方法が経済性の
面からも魅力のあるものとして注目されている。
As a source of carbon dioxide, methods have been proposed such as recovering carbon dioxide from exhaust gas obtained by separately burning fuel, and transporting carbon dioxide gas in carbon dioxide cylinders. The method of using it effectively is attracting attention as it is attractive from an economical point of view.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら淡水化装置から発生する炭酸ガスは、元来
海水中に含まれる重炭酸塩が下記(1)式の反応により
分解して発生するものであり、2HO(h−→Cot 
+ 00g”−+ Hz O・・・・・・・・・・・・
・・・(1)この重炭酸塩濃度が海水の環境すなわち気
温。
However, the carbon dioxide gas generated from desalination equipment is originally generated when bicarbonate contained in seawater is decomposed by the reaction of formula (1) below, and is 2HO (h-→Cot
+ 00g”-+ Hz O・・・・・・・・・・・・
...(1) This bicarbonate concentration is the seawater environment, that is, the temperature.

水温、風速等に左右され必ずしも一定ではない。It is not necessarily constant as it depends on water temperature, wind speed, etc.

加えて前記(1)式の反応速度は温度の、影響を受ける
ため、淡水化装置の運転条件すなわち負荷変動によって
も炭酸ガスの発生量は増減する。
In addition, since the reaction rate of equation (1) is affected by temperature, the amount of carbon dioxide gas generated increases or decreases depending on the operating conditions of the desalination device, that is, load fluctuations.

この結果淡水化装置より発生する炭酸ガス含有ガスの量
及び炭酸ガス濃度が変動してしまう。
As a result, the amount of carbon dioxide-containing gas and the concentration of carbon dioxide gas generated from the desalination device fluctuate.

量又は組成の変動した炭酸ガス含有ガスをそのまま淡水
に吹き込んで炭酸含有水とすれば水中の炭酸濃度も変動
してしまう。生石灰及び/又はドロマイトを充填したフ
ィルター内を前記炭酸含有水が通過すると下記(2)及
びl又は(3)弐に従って溶解するため溶解後の 0a00s+OO*+HtO−Oa(HOOs)x  
 ”・・曲間(21oaIIMg(OOn)* + 2
00t + 2HtOqkJa(HOOs )t +1
4g(aaoait ・・べ3)淡水中のカルシウム及
び/又はマグネシウム。
If a carbon dioxide-containing gas whose amount or composition has changed is directly blown into fresh water to produce carbonated water, the carbon dioxide concentration in the water will also vary. When the carbonated water passes through a filter filled with quicklime and/or dolomite, it dissolves according to (2) and (3) 2 below, so 0a00s + OO * + HtO - Oa (HOOs) x after dissolution.
”...Song interval (21oaIIMg(OOn)* + 2
00t + 2HtOqkJa(HOOs)t +1
4g (aaoait...3) Calcium and/or magnesium in fresh water.

重炭酸根とも炭酸含有水中の炭酸濃度の変動にともなっ
て変動してしまう。
Both bicarbonate roots fluctuate with changes in the carbonate concentration in carbonate-containing water.

処理後飲料水中の上記溶出成分の変動は、処理水の腐食
性を低減し安定化させるという飲料水化本来の目的に逆
行するものであり、飲み味  ′の改善面からみても不
完全である。又、フィルターに充填した石灰石及びl又
はドロマイトの消費量も変動し、補充充填操作面でも不
都合である。蒸発法海水淡水化装置で生成される炭酸・
ガスを利用するシステム自体が比較的新しいものであり
、従来は上記不都合点を解消する方法が見あたらなかっ
た。
The above-mentioned fluctuations in the eluted components in the treated drinking water go against the original purpose of making the treated water into drinking water, which is to reduce and stabilize the corrosivity, and it is also incomplete from the perspective of improving the drinking taste. . Furthermore, the amount of limestone and dolomite filled in the filter varies, which is inconvenient in terms of refilling operations. Carbonic acid produced by evaporative seawater desalination equipment
The system itself that utilizes gas is relatively new, and so far no method has been found to solve the above-mentioned disadvantages.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、上記従来法の問題点を解消するために鋭意研
究の結果見い出されたも9ので、その骨子とするところ
は、フィルター通過後の淡水の比抵抗値が所定値となる
ようフィルター通過前の淡水に吹き込む炭酸ガス含有ガ
スの吹き込み量を調整する淡水の飲料水゛北方法である
The present invention was discovered as a result of intensive research to solve the above-mentioned problems of the conventional method. This is a method for producing fresh drinking water by adjusting the amount of carbon dioxide-containing gas blown into the fresh water.

詳しくは、蒸発法による海水の淡水化装置で生成した淡
水に、該淡水化装置より発生する炭酸ガス含有ガスを吹
き込んで炭酸含有水としたのち、石灰石及びl又はドロ
マイトの粒状物を充填したフィルターを通過させて飲料
水を得る□方法において、フィルター通過後の淡水の比
抵抗値を連続的に検知し、比抵抗値が所定値となるよう
前記炭酸ガス含有ガスの吹き込み量を調整することを特
徴とする淡水の飲料水化方法を提案するものである。
Specifically, fresh water produced by a seawater desalination device using an evaporation method is made into carbonated water by blowing carbon dioxide-containing gas generated from the desalination device, and then filtered with limestone and limestone or dolomite granules. In the □ method for obtaining drinking water by passing the fresh water through the filter, the specific resistance value of the fresh water after passing through the filter is continuously detected, and the amount of the carbon dioxide-containing gas blown is adjusted so that the specific resistance value becomes a predetermined value. This paper proposes a method for converting freshwater into drinking water with its characteristics.

〔作用〕[Effect]

本発明方法では、フィルター出口の処理水中の比抵抗値
を連続的に検知して、この値が所定値となるよう淡水化
装置で発生する炭酸ガス含有ガスをフィルター人口の淡
水に吹き込む量をフィードパラ゛り調整するため、先□
述の原因により前記炭酸ガス含有ガス量又はガス組成が
変動してもフィルター出口の処理水性状を安定に保持で
きる利点をもつ。
In the method of the present invention, the specific resistance value in the treated water at the filter outlet is continuously detected, and the amount of carbon dioxide-containing gas generated in the desalination equipment to be blown into the fresh water in the filter population is fed so that this value becomes a predetermined value. To adjust the parameters, first □
It has the advantage that the properties of the treated water at the filter outlet can be stably maintained even if the amount of carbon dioxide gas or the gas composition changes due to the reasons mentioned above.

本発明者ら社、比抵抗値と液中の溶存成分すなわちカル
シウム、マグネシウム、重炭酸塩濃度には一定の相関が
あり、かつ比抵抗値は従来より一般的に行なわれている
ように電極を対象水中゛に浸すことのみで極めて容易に
連続的に測定することが出来ることに注目し、本発明に
至ったもの−である。すなわちフィルター出口の処理水
性状とは具体的には硬度を増加させるカルシウム及びマ
グネシウムと主として重炭酸機に起因する全アルカリ度
であり、あらかじめ比抵抗値とこれらの値の相関関係を
把握しておくことKより、比抵抗値の測定により上記処
理後の水の性状を連続的に観察することが可能となるこ
とを見い出している。
The present inventors believe that there is a certain correlation between the specific resistance value and the concentration of dissolved components in the liquid, such as calcium, magnesium, and bicarbonate. The present invention was developed based on the fact that continuous measurement can be carried out extremely easily simply by immersing the target in water. In other words, the properties of the treated water at the filter outlet are specifically calcium and magnesium, which increase hardness, and total alkalinity, which is mainly caused by the bicarbonate machine, and it is important to understand the correlation between the specific resistance value and these values in advance. It has been found that it is possible to continuously observe the properties of the water after the above treatment by measuring the specific resistance value.

〔効果〕〔effect〕

本発明方法によれば淡水化発生装置での炭酸ガス発生量
が増加した場合にも、石灰石及び/又はドロマイトが所
定値以上に淡水中に溶解して石灰石、ドロマイトの消費
量を必要以上に増加させることもなく、又炭酸ガス発生
量が減少した場合には炭酸ガス含有ガスの吹き込み量を
増加させることにより所定量の石灰石及び/又はドロマ
イトを溶解させることが出来、淡水の飲料水化が行い得
る。
According to the method of the present invention, even when the amount of carbon dioxide gas generated in the desalination generator increases, limestone and/or dolomite dissolves in the fresh water to a level exceeding a predetermined value, increasing the consumption of limestone and dolomite more than necessary. Moreover, when the amount of carbon dioxide gas generated decreases, by increasing the amount of carbon dioxide-containing gas blown in, a predetermined amount of limestone and/or dolomite can be dissolved, and fresh water can be converted into drinking water. obtain.

〔実施例〕〔Example〕

次に本発明方法の実施態様を明らかにするため、図にも
とすいて説明する。
Next, in order to clarify the embodiment of the method of the present invention, it will be explained with reference to the drawings.

第1図は本発明を海水の多段フラッシュ蒸発法から得ら
れる淡水の飲料化に適用した場合を示す。ラインaより
海水が多段フラッシュ蒸発装置1に供給され製造された
淡水はラインbにより炭酸ガス吸収塔2に圧送される。
FIG. 1 shows the case where the present invention is applied to the drinking of fresh water obtained from a multi-stage flash evaporation method of seawater. Seawater is supplied to the multistage flash evaporator 1 through line a, and the produced fresh water is pumped to the carbon dioxide absorption tower 2 through line b.

一方濃縮された海水はライン0より系外に排出され、蒸
発にともなって発生した炭酸ガス含有ガスのうち、飲料
水化に使用されるガスはラインdを通ってコンプレッサ
ー3により昇圧されたのち流量制御弁7を通過後ライン
fにより炭酸ガス吸収塔2に送入される。余剰の炭酸ガ
ス含有ガスはエジェクター(図示なし)Kよりラインe
を通って系外に排出される。炭酸ガス吸収塔2ではライ
ンbKより送入された淡水に所定量の炭酸ガスが溶解後
ラインhを通ってフィルター4に送り込まれる。未溶解
の炭酸及び窒素、酸素等のガスはラインgJ、り系外に
排出される。炭酸ガス吸収塔2としては充填塔が適用で
きる。
On the other hand, the concentrated seawater is discharged out of the system through line 0, and among the carbon dioxide-containing gases generated as a result of evaporation, the gas used to make drinking water passes through line d and is pressurized by compressor 3, after which the flow rate After passing through the control valve 7, it is sent to the carbon dioxide absorption tower 2 via line f. Excess carbon dioxide-containing gas is discharged from ejector (not shown) K to line e.
is discharged from the system through the In the carbon dioxide absorption tower 2, a predetermined amount of carbon dioxide is dissolved in the fresh water fed through the line bK, and then fed into the filter 4 through the line h. Undissolved carbon dioxide and gases such as nitrogen and oxygen are discharged out of the system via line gJ. As the carbon dioxide absorption tower 2, a packed tower can be used.

また吸収条件によっては吸収塔20代わりにラインミキ
サーの使用も可能である。ラインhより送入された炭酸
含有水はフィルター4内を通過する間にフィルター内に
充てんされた石灰石を溶解し、硬度及び全アルカリ度を
増した後ライン1より抜き出される。ライン1には比抵
抗の検出端5が設置されており処理水の比抵抗が連続的
に測定されその出力は調節計6に入力される。検出端5
としては通常電極が用いられる。
Further, depending on the absorption conditions, a line mixer may be used instead of the absorption tower 20. The carbonated water fed through line h dissolves the limestone filled in the filter while passing through filter 4, increases hardness and total alkalinity, and is then extracted from line 1. A resistivity detection end 5 is installed in the line 1 to continuously measure the resistivity of the treated water and its output is input to a controller 6. Detection end 5
Usually, electrodes are used.

調節計6からはあらかじめ設定しである比抵抗値との差
異に応じた信号がラインkにより出力され吸収塔2に送
入される炭酸ガス含有ガスの流量が調節弁7によって調
節され机すなわち検出端5により測定された比抵抗値が
設定値より小さければ調節弁7が開けられ、比抵抗値が
設定値より高ければ調節弁7が閉じられる。このような
制御により、硬度、全アルカリ、TDS(全溶解固形分
)を所定値に設定された水はライノコより糸外にとり出
される。とり出され水はアルカリを添加されて■を調整
(図示なし)されて腐食性のない安定な水となる。
A signal corresponding to the difference from a preset specific resistance value is outputted from the controller 6 via line k, and the flow rate of the carbon dioxide-containing gas sent to the absorption tower 2 is regulated by the control valve 7. If the resistivity value measured by the end 5 is less than the set value, the regulating valve 7 is opened, and if the resistivity value is higher than the set value, the regulating valve 7 is closed. Through such control, water whose hardness, total alkali, and TDS (total dissolved solids) are set to predetermined values is taken out of the thread from the rhinoceros. The water taken out is added with alkali and adjusted (not shown) to become stable water without corrosive properties.

なお第1図では、多段フラッシュ蒸発装置IKて製造さ
れた淡水全量がラインbにより抜き出されて飲料水化処
理されているが、本発明の適用はこれ゛に限定されるも
のではなく、製造された淡水の一部を飲料水化処理する
場合も適用可能である。
In Fig. 1, the entire amount of fresh water produced by the multi-stage flash evaporator IK is extracted through line b and treated to make it into drinking water, but the application of the present invention is not limited to this, and the production It is also applicable to the case where a part of the fresh water produced is treated to make it into drinking water.

海水の多段フラッシュ蒸発装置1より製造された淡水と
、炭酸ガス含有ガ、スを分取し第1図に示す態様の飲料
水化法により処理した。淡水分取量は20(11’/h
rであり、炭酸ガス含有ガスは第1段目と第7段目より
抽出され、その流量は調節弁7により調節される。吸収
塔7としてはラシヒリング充てん塔を使用し、フィルタ
ー4にはふるい径11IIIから4wmの石灰石を充填
した。
Fresh water and carbon dioxide-containing gas produced by the multi-stage flash evaporation device 1 of seawater were separated and treated by the potable water conversion method shown in FIG. The amount of fresh water extracted is 20 (11'/h
r, and the carbon dioxide-containing gas is extracted from the first stage and the seventh stage, and its flow rate is regulated by the control valve 7. A Raschig ring packed tower was used as the absorption tower 7, and the filter 4 was filled with limestone having a sieve diameter of 11III to 4 wm.

処理後の全硬度がl炭酸カルシウム基準で60wIgμ
となるよう調節計6の設定値を決め、jよりとり出され
る゛製造水の全硬度と全アルカリ度な2時間毎にサンプ
リングした。
Total hardness after treatment is 60wIgμ based on l calcium carbonate.
The setting value of the controller 6 was determined so that

分析結果は次のとおりであった。The analysis results were as follows.

平均値標準偏差 全硬度<21P/l as oaOos) 60.31
.88全アル力リ度 (jlIP# as 0aOOs
)  60.4  1.38なお上記サンプリング期間
に分取した炭酸ガス含有ガス量の平均流量は4.2NZ
/hであった。サンプリング総数は12であった。
Average value standard deviation Total hardness <21P/l as oaOos) 60.31
.. 88 total power level (jlIP# as 0aOOs
) 60.4 1.38 The average flow rate of carbon dioxide-containing gas collected during the above sampling period was 4.2 NZ
/h. The total number of samples was 12.

比較例: 第1図に於いて、調節計6をマニアル設定とし、吸収塔
2に送入する炭酸ガス含有ガス流量を実施例のサンプリ
ング期間中の平均値に固定設定した。他は実施例と全く
同一条件としjよりとり出される製造水の全硬度と全ア
ルカリ度を実施例と同様2時間毎にサンプリングした。
Comparative Example: In FIG. 1, the controller 6 was set to manual, and the flow rate of the carbon dioxide-containing gas fed into the absorption tower 2 was fixed to the average value during the sampling period of the example. The other conditions were exactly the same as in the example, and the total hardness and total alkalinity of the produced water taken out from j were sampled every 2 hours as in the example.

・分析結果は次のとおりであった。・The analysis results were as follows.

平均値 標準偏差 全硬度<”9/l aaσaoos) 58.5 6.
94全アル力リ度(mfll as  0aoos )
  5&8 ’   6.24サンプリング総数は実施
例と同じである。
Average value Standard deviation Total hardness <9/l aaσaoos) 58.5 6.
94 full strength level (mfll as 0aoos)
5 &8' 6.24 The total number of samplings is the same as in the example.

実施例と比較例を比較すると、実施例では処理後の水の
性状が目標値に非常に近くかつ変動が少なく、本発明の
適用による効果が明らかである。
Comparing the Examples and Comparative Examples, the properties of the water after treatment in the Examples are very close to the target values and have little variation, which clearly shows the effects of the application of the present invention.

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

第1図は本発明方法を説明するための回路図である。 1・・・多段フラッシュ蒸発装置、2・・・炭酸ガス吸
収塔、3・・・コンプレッサー、4・・・フィルター、
5・・・比抵抗検出端、6・・・調節計、7・・・流量
調節弁。
FIG. 1 is a circuit diagram for explaining the method of the present invention. 1... Multi-stage flash evaporator, 2... Carbon dioxide absorption tower, 3... Compressor, 4... Filter,
5... Specific resistance detection end, 6... Controller, 7... Flow rate control valve.

Claims (1)

【特許請求の範囲】[Claims] 蒸発法による海水の淡水化装置で生成した淡水に、該淡
水化装置より発生する、炭酸ガス含有ガスを吹き込んで
炭酸含有水としたのち、石灰石及び/又はドロマイトの
粒状物を充填したフィルターを通過させて飲料水を得る
方法において、フィルター通過後の淡水の比抵抗値を連
続的に検知し、比抵抗値が所定値となるよう前記炭酸ガ
ス含有ガスの吹込み量を調整することを特徴とする淡水
の飲料水化方法。
Fresh water produced by a seawater desalination device using the evaporation method is made into carbonated water by blowing carbon dioxide-containing gas generated from the desalination device, and then passed through a filter filled with limestone and/or dolomite granules. In the method for obtaining drinking water, the specific resistance value of the fresh water after passing through the filter is continuously detected, and the amount of the carbon dioxide-containing gas blown is adjusted so that the specific resistance value becomes a predetermined value. A method of converting fresh water into drinking water.
JP16734784A 1984-08-10 1984-08-10 Method for converting freshwater into drinking water Granted JPS6146293A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16734784A JPS6146293A (en) 1984-08-10 1984-08-10 Method for converting freshwater into drinking water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16734784A JPS6146293A (en) 1984-08-10 1984-08-10 Method for converting freshwater into drinking water

Publications (2)

Publication Number Publication Date
JPS6146293A true JPS6146293A (en) 1986-03-06
JPH0361518B2 JPH0361518B2 (en) 1991-09-20

Family

ID=15848041

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16734784A Granted JPS6146293A (en) 1984-08-10 1984-08-10 Method for converting freshwater into drinking water

Country Status (1)

Country Link
JP (1) JPS6146293A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6359393A (en) * 1986-08-30 1988-03-15 Sasakura Eng Co Ltd Method for making mineralized water
JPS6391194A (en) * 1986-10-02 1988-04-21 Sasakura Eng Co Ltd Production of mineralized water from pure water
JPS63141696A (en) * 1986-12-02 1988-06-14 Sasakura Eng Co Ltd Production of mineralized water
EP1382574A2 (en) * 2002-06-21 2004-01-21 Sanden Corporation Mineral water making apparatus
KR100990486B1 (en) 2010-08-18 2010-11-29 케이씨삼양정수(주) Potabilization method and apparatus for producing potable water from desalinated seawater

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6359393A (en) * 1986-08-30 1988-03-15 Sasakura Eng Co Ltd Method for making mineralized water
JPS6391194A (en) * 1986-10-02 1988-04-21 Sasakura Eng Co Ltd Production of mineralized water from pure water
JPS63141696A (en) * 1986-12-02 1988-06-14 Sasakura Eng Co Ltd Production of mineralized water
EP1382574A2 (en) * 2002-06-21 2004-01-21 Sanden Corporation Mineral water making apparatus
EP1382574A3 (en) * 2002-06-21 2004-05-26 Sanden Corporation Mineral water making apparatus
KR100990486B1 (en) 2010-08-18 2010-11-29 케이씨삼양정수(주) Potabilization method and apparatus for producing potable water from desalinated seawater
WO2012023742A2 (en) * 2010-08-18 2012-02-23 Kc Samyang Water Systems Co., Ltd. Potabilization method and apparatus for producing potable water from desalinated seawater
WO2012023742A3 (en) * 2010-08-18 2012-12-27 Kc Samyang Water Systems Co., Ltd. Potabilization method and apparatus for producing potable water from desalinated seawater

Also Published As

Publication number Publication date
JPH0361518B2 (en) 1991-09-20

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