JP3826289B2 - Desalination method - Google Patents
Desalination method Download PDFInfo
- Publication number
- JP3826289B2 JP3826289B2 JP2002242772A JP2002242772A JP3826289B2 JP 3826289 B2 JP3826289 B2 JP 3826289B2 JP 2002242772 A JP2002242772 A JP 2002242772A JP 2002242772 A JP2002242772 A JP 2002242772A JP 3826289 B2 JP3826289 B2 JP 3826289B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- salt
- seawater
- well water
- reverse osmosis
- 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.)
- Expired - Fee Related
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Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、塩分を含む井戸水を原水とする淡水化方法に関する。本発明は、また、海水を原水とする淡水化方法に関する。この明細書において、井戸から得られる塩分を含む水を「塩分含有井戸水」と言う。
【0002】
【従来の技術】
通常、逆浸透法による海水淡水化装置では炭酸カルシウム等のスケール析出防止のために原水に酸を添加してpH調整を行っている。その酸の添加量は主に原水中の重炭酸イオン濃度およびカルシウムイオン濃度により決定される。
【0003】
逆浸透膜供給水のpH調整のための酸添加量は、原水中に重炭酸イオンおよびカルシウムイオンが多いほど増大する。このため、重炭酸イオンやカルシウムイオンの含有量の多い塩分含有井戸水を原水とする淡水化では、多量の酸を添加する必要がある。
【0004】
また、塩分含有井戸水を逆浸透法で処理する場合、逆浸透膜モジュールに供給された同水の一部は濃縮水(ブライン)として放流する必要があるため、生産水量より1〜4割多い塩分含有井戸水を井戸から取水して淡水化装置に供給する必要がある。しかし、多量の塩分含有井戸水を既存の井戸から取得すると、井戸水位の低下や井戸水質の悪化を招くことが懸念される。
【0005】
また、逆浸透法海水淡水化設備では、逆浸透膜のホウ素除去性能の経年変動により透過水中のホウ素濃度が水道水水質基準(ホウ素濃度:1ppm以下)を守れない恐れがある。例えば、ホウ素濃度4ppmの海水を原水とした場合、逆浸透法で得られる透過水のホウ素濃度は1.5ppmである。そのため、ホウ素濃度を水道水水質基準以下に抑えるホウ素除去設備を設置せざるを得ない。しかし、ホウ素除去設備では苛性ソーダを添加してpH調整を行いホウ素を処理する必要があるため、ホウ素除去後の透過水のpHが高くなる。このため、ホウ素除去後の透過水に炭酸ガスや硫酸等を添加してpHを調整し、この水を水道水水質基準に適合させる必要がある。
【0006】
【発明が解決しようとする課題】
本発明は、上記の点に鑑み、スケール形成抑制に必要な酸添加量を低減させることができ、取水量増加に起因する井戸水位低下や水質悪化を招く恐れのない塩分含有井戸水淡水化方法を提供することを目的とする。
【0007】
本発明は、また、ホウ素除去設備を省略もしくは小型化することができる海水淡水化方法を提供することを目的とする。
【0008】
【課題を解決するための手段】
本発明による方法は、カルシウムイオンおよび重炭酸イオンを含み、スケール析出防止のためにpH調整が必要な塩分を含有する井戸水を逆浸透法により淡水化するに当たり、該塩分含有井戸水に海水を混合し、ここで、該井戸水に対する海水の混合割合が20:80〜80:20であることを特徴とする淡水化方法である。
【0011】
【発明の実施の形態】
つぎの、本発明を実施例に基づいて具体的に説明する。
【0012】
実施例1
原水である、260ppmのカルシウムイオンおよび450ppmの重炭酸イオンを含む塩分含有井戸水に海水を下記表1に示す割合で混合し、得られた混合物を逆浸透法により淡水化した。同一回収率(逆浸透膜モジュールへの供給水量に対する生産水量の比率)での必要酸添加量を下記表1に示す。
【0013】
【表1】
【0014】
この表から分かるように、塩分含有井戸水に対する海水の混合割合を増すことにより、酸添加量を大幅に低減できる。
【0015】
実施例2
原水である海水に塩分含有井戸水を1:1の割合で混合し、得られた混合物を逆浸透法により淡水化した。上記混合物のホウ素濃度は3ppmであり、得られた透過水のホウ素濃度は1.0ppm未満であった。
【0016】
【発明の効果】
第一発明では、塩分含有井戸水に海水を混合し、得られた混合物を逆浸透法により淡水化するので、原水中のスケール成分である重炭酸イオンやカルシウムイオン濃度を低減し、スケール形成抑制に必要な酸の添加量を低減させることができる。また、塩分含有井戸水に海水を加えることにより、井戸での取水量を増す必要がないため、取水量増加に起因する井戸水位低下や水質悪化を招くことなく、既設の井戸をそのまま利用することができる。
【0017】
第二発明では、原水である海水に塩分含有井戸水を混合することにより、ホウ素除去設備を省略もしくは小型化することができ、メンテナンスを省略し、pH調整薬品の使用量を低減することができる。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a desalination method using well water containing salt as raw water. The present invention also relates to a desalination method using seawater as raw water. In this specification, water containing salt obtained from a well is referred to as “salt-containing well water”.
[0002]
[Prior art]
Usually, in a seawater desalination apparatus using a reverse osmosis method, pH is adjusted by adding an acid to raw water in order to prevent scale precipitation of calcium carbonate or the like. The amount of acid added is mainly determined by the bicarbonate ion concentration and calcium ion concentration in the raw water.
[0003]
The amount of acid added for adjusting the pH of the reverse osmosis membrane feed water increases as there are more bicarbonate ions and calcium ions in the raw water. For this reason, in desalination using salt-containing well water with a high content of bicarbonate ions and calcium ions as raw water, it is necessary to add a large amount of acid.
[0004]
In addition, when salt-containing well water is treated by the reverse osmosis method, it is necessary to discharge a part of the same water supplied to the reverse osmosis membrane module as concentrated water (brine). Contained well water needs to be taken from the well and supplied to the desalination unit. However, if a large amount of salt-containing well water is acquired from an existing well, there is a concern that the well water level may be lowered or the well water quality may be deteriorated.
[0005]
Moreover, in reverse osmosis seawater desalination facilities, there is a risk that the boron concentration in the permeated water may not comply with the tap water quality standard (boron concentration: 1 ppm or less) due to the aging of the boron removal performance of the reverse osmosis membrane. For example, when seawater having a boron concentration of 4 ppm is used as the raw water, the boron concentration of the permeated water obtained by the reverse osmosis method is 1.5 ppm. Therefore, it is necessary to install a boron removal facility that keeps the boron concentration below the tap water quality standard. However, in the boron removal equipment, it is necessary to adjust the pH by adding caustic soda to treat the boron, so that the pH of the permeated water after boron removal becomes high. For this reason, it is necessary to adjust the pH by adding carbon dioxide gas, sulfuric acid, or the like to the permeated water after boron removal, and to adjust this water to the tap water quality standard.
[0006]
[Problems to be solved by the invention]
In view of the above points, the present invention provides a salt-containing well water desalination method that can reduce the amount of acid addition necessary for suppressing scale formation and that does not cause a decrease in well water level or deterioration in water quality due to an increase in water intake. The purpose is to provide.
[0007]
Another object of the present invention is to provide a seawater desalination method capable of omitting or downsizing a boron removal facility.
[0008]
[Means for Solving the Problems]
How Ru good to the invention comprises a calcium ion and bicarbonate ion, upon desalination by the well water containing salt necessary pH adjustments to prevent scale deposition reverse osmosis, seawater salt content containing well water Here, the desalination method is characterized in that the mixing ratio of seawater to the well water is 20:80 to 80:20 .
[0011]
DETAILED DESCRIPTION OF THE INVENTION
Next, the present invention will be specifically described based on examples.
[0012]
Example 1
Seawater was mixed with the salt-containing well water containing 260 ppm of calcium ions and 450 ppm of bicarbonate ions, which is the raw water, and the resulting mixture was desalinated by the reverse osmosis method. The required acid addition amount at the same recovery rate (ratio of the production water amount to the supply water amount to the reverse osmosis membrane module) is shown in Table 1 below.
[0013]
[Table 1]
[0014]
As can be seen from this table, the amount of acid added can be greatly reduced by increasing the mixing ratio of seawater to the salt-containing well water.
[0015]
Example 2
Salt water containing salt water was mixed at a ratio of 1: 1 with seawater as raw water, and the resulting mixture was desalinated by a reverse osmosis method. The boron concentration of the above mixture was 3 ppm, and the boron concentration of the obtained permeated water was less than 1.0 ppm.
[0016]
【The invention's effect】
In the first invention, seawater is mixed with the salt-containing well water, and the resulting mixture is desalinated by the reverse osmosis method, so the concentration of bicarbonate ions and calcium ions, which are scale components in the raw water, is reduced, and scale formation is suppressed. The required amount of acid added can be reduced. In addition, it is not necessary to increase the water intake in the well by adding seawater to the salt-containing well water, so existing wells can be used as they are without causing a drop in well water level or deterioration in water quality due to an increase in water intake. it can.
[0017]
In the second invention, by mixing the salt-containing well water with the seawater that is the raw water, the boron removal equipment can be omitted or miniaturized, maintenance can be omitted, and the amount of pH adjusting chemical used can be reduced.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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JP2002242772A JP3826289B2 (en) | 2002-08-23 | 2002-08-23 | Desalination method |
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JP2002242772A JP3826289B2 (en) | 2002-08-23 | 2002-08-23 | Desalination method |
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JP2004081903A JP2004081903A (en) | 2004-03-18 |
JP3826289B2 true JP3826289B2 (en) | 2006-09-27 |
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JP2002242772A Expired - Fee Related JP3826289B2 (en) | 2002-08-23 | 2002-08-23 | Desalination method |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102482123A (en) * | 2009-09-08 | 2012-05-30 | 东丽株式会社 | Fresh Water Production Method And Fresh Water Production Device |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4481345B1 (en) * | 2008-11-28 | 2010-06-16 | 株式会社神鋼環境ソリューション | Seawater desalination method and seawater desalination apparatus |
CN102583803B (en) | 2008-11-28 | 2013-10-16 | 株式会社神钢环境舒立净 | Method and apparatus for generating fresh water, and method and apparatus for desalinating sea water |
JP4518435B1 (en) * | 2009-02-13 | 2010-08-04 | 株式会社神鋼環境ソリューション | Seawater desalination method and seawater desalination apparatus |
JP4499835B1 (en) * | 2009-02-14 | 2010-07-07 | 株式会社神鋼環境ソリューション | Fresh water generating apparatus and fresh water generating method |
JP4499834B1 (en) * | 2009-02-14 | 2010-07-07 | 株式会社神鋼環境ソリューション | Fresh water generating apparatus and fresh water generating method |
US20120305459A1 (en) * | 2009-07-21 | 2012-12-06 | Toray Industries, Inc. | Water producing system |
US9309138B2 (en) | 2009-08-21 | 2016-04-12 | Toray Industries, Inc. | Fresh water production method |
EP2468685A4 (en) | 2009-08-21 | 2013-03-13 | Toray Industries | Fresh water generator |
MX2012004104A (en) | 2009-12-25 | 2012-05-29 | Toray Industries | Water production system and operation method therefor. |
JP5119280B2 (en) * | 2010-02-02 | 2013-01-16 | 株式会社神鋼環境ソリューション | Seawater desalination method and seawater desalination apparatus |
JP2010188344A (en) * | 2010-04-05 | 2010-09-02 | Kobelco Eco-Solutions Co Ltd | Method and apparatus of desalinating seawater |
-
2002
- 2002-08-23 JP JP2002242772A patent/JP3826289B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102482123A (en) * | 2009-09-08 | 2012-05-30 | 东丽株式会社 | Fresh Water Production Method And Fresh Water Production Device |
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