JP2003285058A - Salt-containing water desalination system - Google Patents

Salt-containing water desalination system

Info

Publication number
JP2003285058A
JP2003285058A JP2002087725A JP2002087725A JP2003285058A JP 2003285058 A JP2003285058 A JP 2003285058A JP 2002087725 A JP2002087725 A JP 2002087725A JP 2002087725 A JP2002087725 A JP 2002087725A JP 2003285058 A JP2003285058 A JP 2003285058A
Authority
JP
Japan
Prior art keywords
water
salt
containing water
seawater
insoluble matter
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.)
Withdrawn
Application number
JP2002087725A
Other languages
Japanese (ja)
Inventor
Masahiko Nagai
正彦 永井
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 JP2002087725A priority Critical patent/JP2003285058A/en
Publication of JP2003285058A publication Critical patent/JP2003285058A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Filtration Of Liquid (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a system capable of desalting salt-containing water without exerting a bad influence on the surrounding water area. <P>SOLUTION: The seawater desalination system 100 is composed of an intake pump 111 for taking in seawater 1, an insoluble material remover 120 for removing insoluble materials from the intake seawater 1, an desalination device 130 for obtaining clean water 3 and concentrated water 4 by the permeation of the seawater 1 through a reverse osmosis membrane (RO membrane) 132, a sewage treatment device 140 for purifying used sewage 5, and a concentrated water treatment device 150 for mixing the concentrated water 4 and purified water 6 from the sewage treatment device 140 to obtain adjusted water 8 having a salt concentration almost equal to that of the seawater 1. <P>COPYRIGHT: (C)2004,JPO

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、塩分含有水を淡水
化させる塩分含有水淡水化システムに関し、特に、長距
離航行大型客船や離島のリゾートホテル等で海水を淡水
化する場合に適用すると極めて有効なものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a salt-containing water desalination system for desalination of salt-containing water, and particularly when applied to seawater desalination in a long-distance large passenger ship or a resort hotel on a remote island. It is valid.

【0002】[0002]

【従来の技術】長距離を航行するタンカー船やコンテナ
船等の大型船舶においては、乗員の使用する水をタンク
に貯蔵したり、使用した下水を浄化処理して上水として
再び利用するなどしている。他方、旅客者が乗船する豪
華客船等のような長距離航行大型客船においては、下水
を浄化処理した水を飲料水等として使用すると、旅客者
に対して嫌悪感を与える可能性があるため、海水を淡水
化させて上水として使用する海水淡水化システムが搭載
されている。
2. Description of the Related Art In large ships such as tanker ships and container ships that travel long distances, water used by passengers is stored in tanks, used sewage is purified and reused as clean water. ing. On the other hand, in a long-distance large passenger ship such as a luxury passenger ship on which passengers board, using sewage-purified water as drinking water may cause passengers to dislike it. It is equipped with a seawater desalination system that desalinates seawater for use as clean water.

【0003】[0003]

【発明が解決しようとする課題】前述したような海水淡
水化システムにおいては、海水の淡水化の際に副生する
高塩濃度の濃縮水(海水の約1.5〜2.5倍)を海中
に排出する必要がある。しなしながら、高塩濃度の濃縮
水をそのまま戻してしまうと、周辺海域の塩濃度が変化
して、環境的に問題を生じてしまうおそれがあった。
In the seawater desalination system as described above, concentrated salt water having a high salt concentration (about 1.5 to 2.5 times that of seawater) produced as a byproduct during seawater desalination is used. Must be discharged into the sea. However, if the concentrated water having a high salt concentration is returned as it is, the salt concentration in the surrounding sea area may change, which may cause an environmental problem.

【0004】このような問題は、旅客者が乗船する豪華
客船等のような長距離航行大型客船に限らず、例えば、
離島に建設されるリゾートホテル等のように、上水の確
保が困難で環境保全基準が厳しい場所であれば、上述と
同様に生じることである。また、海水に限らず、塩分を
含有する水であれば、上述と同様な問題を生じる可能性
がある。
Such a problem is not limited to a long-distance large cruise ship such as a luxury cruise ship on which passengers board, but for example,
This is the same as above when it is a place where it is difficult to secure clean water and the environmental conservation standards are strict, such as a resort hotel constructed on a remote island. Further, not only seawater but also water containing salt may cause the same problem as described above.

【0005】このようなことから、本発明は、周辺水域
に悪影響を与えることなく塩分含有水を淡水化させるこ
とができる塩分含有水淡水化システムを提供することを
目的とする。
In view of the above, an object of the present invention is to provide a salt-containing water desalination system capable of desalinating salt-containing water without adversely affecting the surrounding water area.

【0006】[0006]

【課題を解決するための手段】前述した課題を解決する
ための、第一番目の発明による塩分含有水淡水化システ
ムは、塩分含有水を取水する取水手段と、取水された前
記塩分含有水を高圧ポンプで逆浸透膜へ透過させて上水
と濃縮水とを得る淡水化手段と、使用された下水を浄化
させる下水処理手段と、前記塩分含有水の塩濃度と略同
等の塩濃度の調整水を得るように前記濃縮水と前記下水
処理手段からの浄化水とを混合して調整する濃縮水処理
手段とを備えたことを特徴とする。
A salt-containing water desalination system according to the first aspect of the present invention for solving the above-mentioned problems comprises an intake means for taking salt-containing water, and the salt-containing water taken up. Desalination means for obtaining clean water and concentrated water by permeating the reverse osmosis membrane with a high-pressure pump, sewage treatment means for purifying used sewage, and adjustment of salt concentration approximately equal to the salt concentration of the salt-containing water. Concentrated water treatment means for mixing and adjusting the concentrated water and purified water from the sewage treatment means so as to obtain water is provided.

【0007】第二番目の発明による塩分含有水淡水化シ
ステムは、第一番目の発明において、前記下水処理手段
が、前記下水の汚濁因子の値を前記塩分含有水と略同等
にするように調整することを特徴とする。
In the salt-containing water desalination system according to the second invention, in the first invention, the sewage treatment means is adjusted so that the value of the pollution factor of the sewage is substantially equal to that of the salt-containing water. It is characterized by doing.

【0008】第三番目の発明による塩分含有水淡水化シ
ステムは、第一番目または第二番目の発明において、取
水された前記塩分含有水から不溶物を除去する不溶物除
去手段を備えると共に、前記濃縮水処理手段が、前記塩
分含有水の不溶物濃度と略同等とするように前記不溶物
を前記調整水に混合して調整することを特徴とする。
The salt-containing water desalination system according to the third aspect of the present invention is the salt-containing water desalination system according to the first or second aspect, further comprising an insoluble matter removing means for removing insoluble matter from the salt-containing water that has been taken. The concentrated water treatment means mixes and adjusts the insoluble matter with the adjusted water so as to have a concentration substantially equal to the insoluble matter concentration of the salt-containing water.

【0009】第四番目の発明による塩分含有水淡水化シ
ステムは、第三番目の発明において、前記不溶物除去手
段が、前記塩分含有水から除去した不溶物を焼却処理し
て減容化させる減容化手段を備えたことを特徴とする。
The salt-containing water desalination system according to a fourth aspect of the present invention is the salt-containing water desalination system according to the third aspect, wherein the insoluble matter removing means incinerates the insoluble matter removed from the salt-containing water to reduce the volume. It is characterized in that it is provided with a capacity-imparting means.

【0010】第五番目の発明による塩分含有水淡水化シ
ステムは、第一番目から第四番目の発明のいずれかにお
いて、前記下水処理手段からの前記浄化水の少なくとも
一部を前記塩分含有水と共に前記淡水化手段の前記高圧
ポンプに送給する再送手段を備えたことを特徴とする。
A salt-containing water desalination system according to a fifth aspect of the invention is the salt-containing water desalination system according to any one of the first to fourth aspects, wherein at least a part of the purified water from the sewage treatment means is combined with the salt-containing water. It is characterized in that it is provided with a resending means for sending the desalination means to the high-pressure pump.

【0011】[0011]

【発明の実施の形態】本発明による塩分含有水淡水化シ
ステムの実施の形態を図面を用いて説明するが、本発明
は以下の実施の形態に限定されるものではない。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of a salt-containing water desalination system according to the present invention will be described with reference to the drawings, but the present invention is not limited to the following embodiments.

【0012】[第一番目の実施の形態]本発明による塩
分含有水淡水化システムを海水淡水化システムに適用し
た第一番目の実施の形態を図1を用いて説明する。図1
は、海水淡水化システムの概略構成図である。
[First Embodiment] A first embodiment in which the salt-containing water desalination system according to the present invention is applied to a seawater desalination system will be described with reference to FIG. Figure 1
FIG. 1 is a schematic configuration diagram of a seawater desalination system.

【0013】図1に示すように、本実施の形態にかかる
海水淡水化システム100は、海水1を取水する取水手
段である取水ポンプ111と、取水された海水1から不
溶物2を除去する不溶物除去手段である不溶物除去装置
120と、前記海水1を高圧ポンプ131により逆浸透
膜(RO膜)132へ透過させて上水3と濃縮水4とを
得る淡水化手段である淡水化装置130と、使用された
下水5を浄化させる下水処理手段である下水処理装置1
40と、海水1の塩濃度と略同等の塩濃度の調整水8を
得るように濃縮水4と下水処理装置140からの浄化水
6とを混合して調整する濃縮水処理手段である濃縮水処
理装置150とを備えている。
As shown in FIG. 1, a seawater desalination system 100 according to the present embodiment includes an intake pump 111 which is an intake means for taking in seawater 1 and an insoluble material for removing insoluble matter 2 from the taken seawater 1. An insoluble matter removing device 120 which is a substance removing device, and a desalination device which is a desalination device which obtains clean water 3 and concentrated water 4 by permeating the seawater 1 to a reverse osmosis membrane (RO membrane) 132 by a high pressure pump 131. 130 and a sewage treatment device 1 which is a sewage treatment means for purifying the used sewage 5.
40 and concentrated water as a concentrated water treatment means for mixing and adjusting the concentrated water 4 and the purified water 6 from the sewage treatment device 140 so as to obtain the adjusted water 8 having a salt concentration substantially equal to the salt concentration of the seawater 1. And a processing device 150.

【0014】前記不溶物除去装置120は、取水された
海水1を濾過する濾過手段である濾過器121と、濾別
された不溶物2を貯蔵する不溶物貯蔵タンク122とを
備えている。
The insoluble matter removing device 120 comprises a filter 121 which is a filtering means for filtering the taken seawater 1, and an insoluble matter storage tank 122 for storing the filtered insoluble matter 2.

【0015】前記淡水化装置130は、前記高圧ポンプ
131と、前記RO膜132と、前記上水3を貯蔵する
上水貯蔵タンク133と、上水3を使用設備10に供給
する給水手段である給水ポンプ134と、濃縮水4を貯
蔵する濃縮水貯蔵タンク135とを備えている。
The desalination apparatus 130 is a high-pressure pump 131, the RO membrane 132, a clean water storage tank 133 for storing the clean water 3, and a water supply means for supplying the clean water 3 to the facility 10. A water supply pump 134 and a concentrated water storage tank 135 that stores the concentrated water 4 are provided.

【0016】前記下水処理装置140は、使用設備10
からの下水5を貯蔵する下水貯蔵タンク141と、下水
タンク141内の下水5を送出する下水送給手段である
下水送給ポンプ142と、下水送給ポンプ142からの
下水5を浄化させる浄化手段である浄化装置143と、
浄化水6を貯蔵する浄化水貯蔵タンク144と、下水5
の浄化処理に伴って生じた固体分7を貯蔵する固体分貯
蔵タンク145とを備えている。
The sewage treatment equipment 140 is used in the equipment 10
From the sewage storage tank 141 for storing the sewage 5 from the sewage, a sewage feed pump 142 which is a sewage feed means for sending the sewage 5 in the sewage tank 141, and a purification means for purifying the sewage 5 from the sewage feed pump 142 A purifying device 143 which is
Purified water storage tank 144 for storing purified water 6 and sewage 5
And a solid content storage tank 145 for storing the solid content 7 generated by the purification process.

【0017】前記濃縮水処理装置150は、攪拌翼15
1aを備えた調整槽151と、前記淡水化装置130の
前記濃縮水貯蔵タンク135内の濃縮水4を調整槽15
1内に送給する濃縮水送給手段である濃縮水送給ポンプ
152と、前記下水処理装置140の前記浄化水貯蔵タ
ンク144内の浄化水6を調整槽151内に送給する浄
化水送給手段である浄化水送給ポンプ153と、前記取
水ポンプ111の取込口近傍に設けられて塩濃度を計測
する電気伝導度計等の海水塩濃度計測手段である海水塩
濃度計測器154と、前記淡水化装置130の前記濃縮
水貯蔵タンク135に取り付けられて濃縮水4の塩濃度
を計測する電気伝導度計等のような濃縮水濃度計測手段
である濃縮水塩濃度計測器155と、前記調整槽151
内に設けられて調整水8の塩濃度を計測する電気伝導度
計等のような調整水塩濃度計測手段である調整水塩濃度
計測器156と、前記塩濃度計測器154〜156から
の信号に基づいて、前記調整槽151内の調整水8が海
水1と略同等の塩濃度となるように前記送給ポンプ15
2,153を制御する制御手段である制御装置157
と、調整槽151内の調整水8を海中へ排出する排水ポ
ンプ158とを備えている。
The concentrated water treatment device 150 includes a stirring blade 15
1a and an adjusting tank 15 for adjusting the concentrated water 4 in the concentrated water storage tank 135 of the desalination apparatus 130.
1 and a purified water feed pump 152 for feeding the purified water 6 in the purified water storage tank 144 of the sewage treatment apparatus 140 into the adjusting tank 151. A purified water feed pump 153 that is a supply means, and a seawater salt concentration measuring device 154 that is a seawater salt concentration measuring means such as an electric conductivity meter that is provided in the vicinity of the intake port of the water intake pump 111 to measure salt concentration. A concentrated water salt concentration measuring instrument 155, which is a concentrated water concentration measuring means such as an electric conductivity meter attached to the concentrated water storage tank 135 of the desalination apparatus 130 and measuring the salt concentration of the concentrated water 4; The adjusting tank 151
Signals from the adjusted water salt concentration measuring device 156, which is a adjusted water salt concentration measuring means such as an electric conductivity meter or the like provided inside the measuring device, to measure the salt concentration of the adjusted water 8 and the salt concentration measuring devices 154-156. Based on the above, the feed pump 15 is adjusted so that the adjusted water 8 in the adjusting tank 151 has a salt concentration substantially equal to that of the seawater 1.
2, 153, which is a control unit for controlling
And a drainage pump 158 for discharging the adjusted water 8 in the adjusting tank 151 into the sea.

【0018】このような海水淡水化システム100は、
以下のようにして運転される。
Such a seawater desalination system 100 is
It is operated as follows.

【0019】取水ポンプ111で海水1を取水すると、
海水1は、不溶物除去装置120の濾過器121で不溶
物2を除去された後、淡水化装置130の高圧ポンプ1
31でRO膜132に高圧(約4〜10MPa程度)で
送給され、一部が濾過されて淡水化された上水3として
上水貯蔵タンク133に貯蔵され、残りが濃縮水4とし
て濃縮水貯蔵タンク135に貯蔵される。なお、上記濾
過器121で除去された前記不溶物2は、不溶物貯蔵タ
ンク122内に貯蔵される。
When the seawater 1 is taken in by the water intake pump 111,
The seawater 1 is the high pressure pump 1 of the desalination apparatus 130 after the insoluble matter 2 is removed by the filter 121 of the insoluble matter removal apparatus 120.
At 31, a high pressure (about 4 to 10 MPa) is supplied to the RO membrane 132, and a part of the water is filtered and desalinated to be stored in the clean water storage tank 133, and the rest is concentrated water 4 to be concentrated water. It is stored in the storage tank 135. The insoluble matter 2 removed by the filter 121 is stored in the insoluble matter storage tank 122.

【0020】前記上水貯蔵タンク133内の上水3は、
飲料水等の各種生活用水として使用設備10で適宜利用
された後、下水5として下水処理装置140の下水貯蔵
タンク141内に貯蔵される。
The clean water 3 in the clean water storage tank 133 is
After being appropriately used as various domestic water such as drinking water in the facility 10, the sewage 5 is stored in the sewage storage tank 141 of the sewage treatment apparatus 140.

【0021】前記下水貯蔵タンク141内の下水5は、
下水送給ポンプ142により浄化装置143に送給され
て浄化処理された後、浄化水6として浄化水貯蔵タンク
144内に貯蔵される。なお、下水5の浄化処理に伴っ
て発生した固体分7は、固体分貯蔵タンク145内に貯
蔵される。
The sewage 5 in the sewage storage tank 141 is
After being sent to the purification device 143 by the sewage supply pump 142 and subjected to purification treatment, the purified water 6 is stored in the purified water storage tank 144. The solid content 7 generated by the purification process of the sewage 5 is stored in the solid content storage tank 145.

【0022】他方、前記濃縮水処理装置150の制御装
置157は、海水塩濃度計測器154による海水1の塩
濃度計測結果および濃縮水塩濃度計測器155による前
記濃縮水貯蔵タンク135内の濃縮水4の塩濃度計測結
果に基づき、海水1と略同等の塩濃度の調整水8を得る
ように、濃縮水送給ポンプ152および浄化水送給ポン
プ153を作動させて、調整槽151内に濃縮水4およ
び浄化水6を供給し、攪拌翼151aを作動させて混合
調整する。
On the other hand, the controller 157 of the concentrated water treatment device 150 controls the salt concentration measurement result of the seawater 1 by the seawater salt concentration measuring device 154 and the concentrated water in the concentrated water storage tank 135 by the concentrated water concentration measuring device 155. Based on the salt concentration measurement result of No. 4, the concentrated water feed pump 152 and the purified water feed pump 153 are operated so as to obtain the adjusted water 8 having a salt concentration almost equal to that of the seawater 1, and the concentrated water is concentrated in the adjustment tank 151. Water 4 and purified water 6 are supplied, and stirring blade 151a is operated to perform mixing adjustment.

【0023】このとき、制御装置157は、調整水塩濃
度計測器156による調整槽151内の調整水8の塩濃
度の計測結果に基づき、当該調整水8の塩濃度が海水1
の塩濃度と略同等であるかどうか確認し、濃縮水送給ポ
ンプ152および浄化水送給ポンプ153をフィードバ
ック制御を行う。
At this time, the control device 157 determines that the salt concentration of the adjusted water 8 is seawater 1 based on the measurement result of the salt concentration of the adjusted water 8 in the adjusting tank 151 by the adjusted water salt concentration measuring device 156.
It is confirmed whether the salt concentration is substantially equal to the salt concentration, and the concentrated water feed pump 152 and the purified water feed pump 153 are feedback-controlled.

【0024】このようにして調整された調整水8は、排
出ポンプ158の作動により、調整槽151内から海中
へ排出される。
The adjusted water 8 thus adjusted is discharged into the sea from the adjusting tank 151 by the operation of the discharge pump 158.

【0025】したがって、本実施の形態の海水淡水化シ
ステム100によれば、海水1の淡水化の際に副生する
高塩濃度の濃縮水4を、下水5を浄化した浄化水6と混
合して海水1の塩濃度と略同等の調整水8にしてから海
中に排出するようにしたので、周辺海域の塩濃度に変化
を与えることがなく海水を淡水化させることができ、環
境的に生じる問題を大幅に低減することができる。
Therefore, according to the seawater desalination system 100 of the present embodiment, the concentrated water 4 having a high salt concentration, which is a by-product during the desalination of the seawater 1, is mixed with the purified water 6 obtained by purifying the sewage 5. Since the adjusted water 8 which is almost equivalent to the salt concentration of the seawater 1 is discharged into the sea, the seawater can be desalinated without changing the salt concentration in the surrounding sea area, which is environmentally generated. The problem can be greatly reduced.

【0026】特に、このような海水淡水化システム10
0を、旅客者が乗船する豪華客船等のような長距離航行
大型客船を始めとして、例えば、離島に建設されるリゾ
ートホテル等のように、上水の確保が困難で環境保全基
準が厳しい場所に適用すると、極めて有効である。
In particular, such a seawater desalination system 10
0 is a place where it is difficult to secure clean water and strict environmental conservation standards, such as large-scale long-distance passenger ships such as luxury passenger ships on which passengers board, and resort hotels that are constructed on remote islands. It is extremely effective when applied to.

【0027】[第二番目の実施の形態]本発明による塩
分含有水淡水化システムを海水淡水化システムに適用し
た場合の第二番目の実施の形態を図2を用いて説明す
る。図2は、海水淡水化システムの概略構成図である。
ただし、前述した第一番目の実施の形態の場合と同様な
部分については、前述した第一番目の実施の形態の説明
で用いた符号と同一の符号を用いることにより、前述し
た第一番目の実施での説明と重複する説明を省略する。
[Second Embodiment] A second embodiment in which the salt-containing water desalination system according to the present invention is applied to a seawater desalination system will be described with reference to FIG. FIG. 2 is a schematic configuration diagram of a seawater desalination system.
However, for the same parts as in the case of the first embodiment described above, by using the same reference numerals as those used in the description of the first embodiment described above, Descriptions that are the same as those in the implementation will be omitted.

【0028】図2に示すように、本実施の形態にかかる
海水淡水化システム200は、海水1を取水する取水手
段である取水ポンプ111と、取水された海水1から不
溶物2を除去する不溶物除去手段である不溶物除去装置
120と、前記海水1を高圧ポンプ131により逆浸透
膜(RO膜)132へ透過させて上水3と濃縮水4とを
得る淡水化手段である淡水化装置130と、使用された
下水5を浄化させる下水処理手段である下水処理装置1
40と、海水1の塩濃度と略同等の塩濃度の調整水8を
得るように濃縮水4と下水処理装置140からの浄化水
6とを混合して調整する濃縮水処理手段である濃縮水処
理装置150と、下水処理装置130からの浄化水6の
少なくとも一部を海水1と共に淡水化装置130の高圧
ポンプ131に送給する再送手段である再送ライン26
1、切替バルブ262等を備えている。
As shown in FIG. 2, the seawater desalination system 200 according to the present embodiment has an intake pump 111 which is an intake means for taking in the seawater 1 and an insoluble material for removing the insoluble matter 2 from the taken seawater 1. An insoluble matter removing device 120 which is a substance removing device, and a desalination device which is a desalination device which obtains clean water 3 and concentrated water 4 by permeating the seawater 1 to a reverse osmosis membrane (RO membrane) 132 by a high pressure pump 131. 130 and a sewage treatment device 1 which is a sewage treatment means for purifying the used sewage 5.
40 and concentrated water as a concentrated water treatment means for mixing and adjusting the concentrated water 4 and the purified water 6 from the sewage treatment device 140 so as to obtain the adjusted water 8 having a salt concentration substantially equal to the salt concentration of the seawater 1. The treatment device 150 and a re-sending line 26 which is a resending means for sending at least a part of the purified water 6 from the sewage treatment device 130 to the high-pressure pump 131 of the desalination device 130 together with the seawater 1.
1, a switching valve 262 and the like.

【0029】前記再送ライン261は、一端が前記濃縮
水処理装置150の浄化水送給ポンプ153の送出口近
傍に切替バルブ262を介して連結され、他端が前記淡
水化装置130の高圧ポンプ131の受入口近傍に連結
されている。
One end of the re-sending line 261 is connected to the vicinity of the outlet of the purified water supply pump 153 of the concentrated water treatment device 150 via a switching valve 262, and the other end is connected to the high pressure pump 131 of the desalination device 130. Is connected near the entrance.

【0030】つまり、本実施の形態による海水淡水化シ
ステム200は、第一番目の実施の形態の海水淡水化シ
ステム100において、前記再送手段を設けた構造とな
っているのである。
That is, the seawater desalination system 200 according to this embodiment has a structure in which the resending means is provided in the seawater desalination system 100 according to the first embodiment.

【0031】このような海水淡水化システム200にお
いては、前記切替バルブ262により、前記下水処理装
置140の浄化水貯蔵タンク153内の浄化水6を前記
再送ライン261を介して高圧ポンプ131の受入口近
傍に送給すると、海水1が浄化水6と混合されてから、
淡水化装置130の高圧ポンプ131によりRO膜13
2へ供給されるようになる。
In such a seawater desalination system 200, the switching valve 262 allows the purified water 6 in the purified water storage tank 153 of the sewage treatment apparatus 140 to be received through the re-sending line 261 into the high pressure pump 131. When it is sent to the vicinity, after the seawater 1 is mixed with the purified water 6,
The high-pressure pump 131 of the desalination apparatus 130 is used for the RO membrane
2 will be supplied.

【0032】ここで、高圧ポンプ131は、RO膜13
2に供給する上記海水1が浄化水6と混合されて塩濃度
を低減されていることから、当該海水1をRO膜132
に供給する供給圧力が小さくて済むようになる。
Here, the high-pressure pump 131 is the RO membrane 13
Since the seawater 1 supplied to the water 2 is mixed with the purified water 6 to reduce the salt concentration, the seawater 1 is supplied to the RO membrane 132.
The supply pressure to be supplied to will be small.

【0033】具体的には、例えば、海水1と浄化水6と
を4:1の割合で混合すれば、塩濃度を4/5程度に低
減することができるので、高圧ポンプ131による送給
圧力を9/10程度にまで小さくすることができる。
Specifically, for example, if seawater 1 and purified water 6 are mixed at a ratio of 4: 1, the salt concentration can be reduced to about 4/5. Can be reduced to about 9/10.

【0034】したがって、本実施の形態の海水淡水化シ
ステム200によれば、前述した第一番目の実施の形態
の場合と同様な効果を得ることができるのはもちろんの
こと、高圧ポンプ131の運転動力を削減することがで
きるので(約9/10程度)、エネルギの有効利用を図
ることができる。
Therefore, according to the seawater desalination system 200 of the present embodiment, the same effects as in the case of the first embodiment described above can be obtained, and the operation of the high-pressure pump 131 can be performed. Since the power can be reduced (about 9/10), the energy can be effectively used.

【0035】特に、旅客者が乗船する豪華客船等のよう
な長距離航行大型客船を始めとして、例えば、離島に建
設されるリゾートホテル等のように、動力エネルギの確
保に限界がある場所に適用すると、極めて有効である。
Particularly, it is applied to a place where there is a limit in securing motive energy, such as a long-distance large passenger ship such as a luxury passenger ship on which passengers board, and a resort hotel constructed on a remote island. Then, it is extremely effective.

【0036】[他の実施の形態]なお、前述した第一、
二番目の実施の形態において、下水処理装置140が、
下水5のCODやBODやTOCやT−N(トータル窒
素量)やT−P(トータル燐量)等の汚濁因子の値を海
水1と略同一にするようにさらに調整するようにすれ
ば、調整水8の水質を海水1にさらに近づけることがで
きるので、環境的に生じる問題をさらに低減することが
できる。
[Other Embodiments] Incidentally, the above-mentioned first,
In the second embodiment, the sewage treatment device 140 is
If the values of pollution factors such as COD, BOD, TOC, TN (total nitrogen content) and TP (total phosphorus content) of the sewage 5 are adjusted to be substantially the same as the seawater 1, Since the quality of the adjusted water 8 can be made closer to that of the seawater 1, environmental problems can be further reduced.

【0037】また、前述した第一、二番目の実施の形態
において、海水1の不溶物2の濃度と略同等とするよう
に不溶物2を調整水8に混合して調整する、具体的に
は、例えば、海水1の濁度を計測する海水濁度計測手段
を前記取水ポンプ111の取込口近傍に設けると共に、
調整水8の濁度を計測する調整水濁度計測手段を前記調
整槽151に設け、前記濁度計測手段での計測結果に基
づいて、調整槽151内の調整水8の濁度が海水1と略
同等となるように前記不溶物貯蔵タンク122内の不溶
物2を調整槽151内に供給すれば、前記不溶物貯蔵タ
ンク122内に貯蔵保管しておく不溶物2の量を大幅に
低減させることができるので、さらに好ましい結果を得
ることができる。
In the first and second embodiments described above, the insoluble matter 2 is mixed with the adjusted water 8 to be adjusted so as to have a concentration substantially equal to the concentration of the insoluble matter 2 in the seawater 1. Is, for example, provided with seawater turbidity measuring means for measuring the turbidity of the seawater 1 in the vicinity of the intake port of the intake pump 111,
Adjusted water turbidity measuring means for measuring the turbidity of the adjusted water 8 is provided in the adjusting tank 151, and the turbidity of the adjusted water 8 in the adjusting tank 151 is seawater 1 based on the measurement result of the turbidity measuring means. If the insoluble matter 2 in the insoluble matter storage tank 122 is supplied to the adjusting tank 151 so as to be substantially equivalent to the above, the amount of the insoluble matter 2 stored and stored in the insoluble matter storage tank 122 is significantly reduced. Therefore, more preferable results can be obtained.

【0038】また、前述した第一,二番目の実施の形態
において、前記不溶物除去装置120が、海水1から除
去した不溶物2を焼却処理して減容化させる減容化手段
を備えれば、貯蔵保管しておく不溶物2の量を大幅に低
減させることができるので、さらに好ましい結果を得る
ことができる。
Further, in the first and second embodiments described above, the insoluble matter removing device 120 is provided with a volume reducing means for incinerating the insoluble matter 2 removed from the seawater 1 to reduce the volume. In this case, the amount of the insoluble matter 2 to be stored and stored can be greatly reduced, so that a more preferable result can be obtained.

【0039】ここで、焼却処理して減容化した不溶物2
を調整槽151内に供給するようにすれば、さらに好ま
しい結果を得ることができる。
Here, insoluble matter 2 reduced in volume by incineration treatment
If it is supplied into the adjusting tank 151, more preferable results can be obtained.

【0040】[0040]

【発明の効果】第一番目の発明による塩分含有水淡水化
システムは、塩分含有水を取水する取水手段と、取水さ
れた前記塩分含有水を高圧ポンプで逆浸透膜へ透過させ
て上水と濃縮水とを得る淡水化手段と、使用された下水
を浄化させる下水処理手段と、前記塩分含有水の塩濃度
と略同等の塩濃度の調整水を得るように前記濃縮水と前
記下水処理手段からの浄化水とを混合して調整する濃縮
水処理手段とを備えたことから、塩分含有水の淡水化の
際に副生する高塩濃度の濃縮水を、下水を浄化した浄化
水と混合して塩分含有水の塩濃度と略同等の調整水にし
てから排出するこができるので、周辺水域の塩濃度に変
化を与えることがなく塩分含有水を淡水化させることが
でき、環境的に生じる問題を大幅に低減することができ
る。
The salinity-containing water desalination system according to the first aspect of the present invention is a water intake means for taking in the salt-containing water, and the salt-containing water thus taken in is passed through the reverse osmosis membrane with a high-pressure pump to obtain clean water. Desalination means for obtaining concentrated water, sewage treatment means for purifying used sewage, and the concentrated water and the sewage treatment means so as to obtain adjusted water having a salt concentration substantially equal to the salt concentration of the salt-containing water. Since a concentrated water treatment means for mixing and adjusting the purified water from the above is provided, the concentrated water having a high salt concentration, which is a by-product during desalination of salt-containing water, is mixed with the purified water obtained by purifying the sewage. Since it can be discharged after making adjusted water that is approximately equivalent to the salt concentration of the salt-containing water, the salt-containing water can be desalinated without changing the salt concentration of the surrounding water area, which is environmentally friendly. The problems that occur can be greatly reduced.

【0041】第二番目の発明による塩分含有水淡水化シ
ステムは、第一番目の発明において、前記下水処理手段
が、前記下水の汚濁因子の値を前記塩分含有水と略同等
にするように調整するので、調整水の水質を塩分含有水
にさらに近づけることができ、環境的に生じる問題をさ
らに低減することができる。
The salt-containing water desalination system according to the second invention is the salt-containing water desalination system according to the first invention, wherein the sewage treatment means adjusts the value of the pollution factor of the sewage to be substantially equal to that of the salt-containing water. Therefore, the quality of the conditioned water can be made closer to that of the salt-containing water, and the environmental problems can be further reduced.

【0042】第三番目の発明による塩分含有水淡水化シ
ステムは、第一番目または第二番目の発明のいずれかに
おいて、取水された前記塩分含有水から不溶物を除去す
る不溶物除去手段を備えると共に、前記濃縮水処理手段
が、前記塩分含有水の不溶物濃度と略同等とするように
前記不溶物を前記調整水に混合して調整するので、貯蔵
保管しておく不溶物の量を大幅に低減させることができ
る。
The salt-containing water desalination system according to the third aspect of the present invention is, in either of the first or second aspects, provided with an insoluble matter removing means for removing insoluble matter from the salt-containing water taken up. At the same time, the concentrated water treatment means adjusts the insoluble matter by mixing the adjusted water with the adjusted water so that the concentration of the insoluble matter in the salt-containing water is substantially equal to the concentration of the insoluble matter. Can be reduced to

【0043】第四番目の発明による塩分含有水淡水化シ
ステムは、第三番目の発明において、前記不溶物除去手
段が、前記塩分含有水から除去した不溶物を焼却処理し
て減容化させる減容化手段を備えたので、貯蔵保管して
おく不溶物の量を大幅に低減させることができる。
A salt-containing water desalination system according to a fourth aspect of the present invention is the salt-containing water desalination system according to the third aspect, wherein the insoluble matter removing means incinerates the insoluble matter removed from the salt-containing water to reduce the volume. Since the volatilization means is provided, the amount of insoluble matter to be stored and stored can be greatly reduced.

【0044】第五番目の発明による塩分含有水淡水化シ
ステムは、第一番目から第四番目の発明のいずれかにお
いて、前記下水処理手段からの前記浄化水の少なくとも
一部を前記塩分含有水と共に前記淡水化手段の前記高圧
ポンプに送給する再送手段を備えたことから、塩分含有
水を逆浸透膜に供給する高圧ポンプの供給圧力を小さく
することができるので、高圧ポンプの運転動力を削減す
ることができ、エネルギの有効利用を図ることができ
る。
A salt-containing water desalination system according to a fifth aspect of the present invention is the salt-containing water desalination system according to any one of the first to fourth aspects, wherein at least a part of the purified water from the sewage treatment means is combined with the salt-containing water. Since the re-sending unit for sending the desalination unit to the high-pressure pump is provided, the supply pressure of the high-pressure pump for supplying the salt-containing water to the reverse osmosis membrane can be reduced, so that the operating power of the high-pressure pump is reduced. Therefore, energy can be effectively used.

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

【図1】本発明による塩分含有水淡水化システムを海水
淡水化システムに適用した場合の第一番目の実施の形態
の概略構成図である。
FIG. 1 is a schematic configuration diagram of a first embodiment when a salt-containing water desalination system according to the present invention is applied to a seawater desalination system.

【図2】本発明による塩分含有水淡水化システムを海水
淡水化システムに適用した場合の第二番目の実施の形態
の概略構成図である。
FIG. 2 is a schematic configuration diagram of a second embodiment when the salt-containing water desalination system according to the present invention is applied to a seawater desalination system.

【符号の説明】 1 海水 2 不溶物 3 上水 4 濃縮水 5 下水 6 浄化水 7 固体分 8 調整水 10 使用設備 100 海水淡水化システム 111 取水ポンプ 120 不溶物除去装置 121 濾過器 122 不溶物貯蔵タンク 130 淡水化装置 131 高圧ポンプ 132 逆浸透膜(RO膜) 133 上水貯蔵タンク 134 給水ポンプ 135 濃縮水貯蔵タンク 140 下水処理装置 141 下水貯蔵タンク 142 下水送給ポンプ 143 浄化装置 144 浄化水貯蔵タンク 145 固体分貯蔵タンク 150 濃縮水処理装置 151 調整槽 151a 攪拌翼 152 濃縮水送給ポンプ 153 浄化水送給ポンプ 154 海水塩濃度計測器 155 濃縮水塩濃度計測器 156 調整水塩濃度計測器 157 制御装置 158 排水ポンプ 200 海水淡水化システム 261 再送ライン 262 切替バルブ[Explanation of symbols] 1 seawater 2 Insoluble matter 3 clean water 4 concentrated water 5 sewage 6 purified water 7 solids 8 adjusted water 10 Equipment used 100 seawater desalination system 111 Water intake pump 120 Insoluble matter removal device 121 Filter 122 Insoluble matter storage tank 130 Desalination equipment 131 High pressure pump 132 Reverse osmosis membrane (RO membrane) 133 clean water storage tank 134 Water supply pump 135 Concentrated water storage tank 140 Sewage treatment equipment 141 Sewage storage tank 142 Sewer pump 143 Purification device 144 Purified water storage tank 145 Solid content storage tank 150 Concentrated water treatment device 151 adjustment tank 151a Stirrer 152 Concentrated water feed pump 153 Purified water feed pump 154 Seawater salt concentration measuring instrument 155 Concentrated water salt concentration measuring instrument 156 Adjusted water salt concentration measuring instrument 157 Control device 158 drainage pump 200 Seawater desalination system 261 Retransmission line 262 Switching valve

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 塩分含有水を取水する取水手段と、 取水された前記塩分含有水を高圧ポンプで逆浸透膜へ透
過させて上水と濃縮水とを得る淡水化手段と、 使用された下水を浄化させる下水処理手段と、 前記塩分含有水の塩濃度と略同等の塩濃度の調整水を得
るように前記濃縮水と前記下水処理手段からの浄化水と
を混合して調整する濃縮水処理手段とを備えたことを特
徴とする塩分含有水淡水化システム。
1. A desalination means for taking in salt-containing water, a desalination means for permeating the taken-in salt-containing water to a reverse osmosis membrane with a high-pressure pump to obtain clean water and concentrated water, and used sewage And a concentrated water treatment for mixing and adjusting the concentrated water and the purified water from the sewage processing means so as to obtain adjusted water having a salt concentration substantially equal to the salt concentration of the salt-containing water. And a salt-containing water desalination system.
【請求項2】 請求項1において、 前記下水処理手段が、前記下水の汚濁因子の値を前記塩
分含有水と略同等にするように調整することを特徴とす
る塩分含有水淡水化システム。
2. The salt-containing water desalination system according to claim 1, wherein the sewage treatment means adjusts the value of the pollution factor of the sewage to be substantially equal to that of the salt-containing water.
【請求項3】 請求項1または請求項2のいずれかにお
いて、 取水された前記塩分含有水から不溶物を除去する不溶物
除去手段を備えると共に、 前記濃縮水処理手段が、前記塩分含有水の不溶物濃度と
略同等とするように前記不溶物を前記調整水に混合して
調整することを特徴とする塩分含有水淡水化システム。
3. The insoluble matter removing device according to claim 1, further comprising an insoluble matter removing device that removes insoluble matter from the salt-containing water that has been taken in, and the concentrated water treating device has the salt-containing water. A salt-containing water desalination system, characterized in that the insoluble matter is mixed with the adjusted water so as to have a concentration substantially equal to that of the insoluble matter.
【請求項4】 請求項3において、 前記不溶物除去手段が、前記塩分含有水から除去した不
溶物を焼却処理して減容化させる減容化手段を備えたこ
とを特徴とする塩分含有水淡水化システム。
4. The salt-containing water according to claim 3, wherein the insoluble matter removing means includes a volume reducing means for incinerating the insoluble matter removed from the salt-containing water to reduce the volume. Desalination system.
【請求項5】 請求項1から請求項4のいずれかにおい
て、 前記下水処理手段からの前記浄化水の少なくとも一部を
前記塩分含有水と共に前記淡水化手段の前記高圧ポンプ
に送給する再送手段を備えたことを特徴とする塩分含有
水淡水化システム。
5. The resending means for sending at least part of the purified water from the sewage treatment means to the high-pressure pump of the desalination means together with the salt-containing water according to any one of claims 1 to 4. A salt-containing water desalination system comprising:
JP2002087725A 2002-03-27 2002-03-27 Salt-containing water desalination system Withdrawn JP2003285058A (en)

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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007513759A (en) * 2003-12-11 2007-05-31 ウォーター スタンダード カンパニー エルエルシー Movable desalination system and method
JP2010149123A (en) * 2008-11-28 2010-07-08 Kobelco Eco-Solutions Co Ltd Seawater desalination method and seawater desalination apparatus
CN102320674A (en) * 2011-06-08 2012-01-18 集美大学 Marine cold and heat cogeneration seawater desalting method and equipment
AU2009320741B2 (en) * 2008-11-28 2012-03-15 Kobelco Eco-Solutions Co., Ltd. Generation of fresh water
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