JP3527466B2 - Deep ocean water treatment plant - Google Patents

Deep ocean water treatment plant

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Publication number
JP3527466B2
JP3527466B2 JP2000249517A JP2000249517A JP3527466B2 JP 3527466 B2 JP3527466 B2 JP 3527466B2 JP 2000249517 A JP2000249517 A JP 2000249517A JP 2000249517 A JP2000249517 A JP 2000249517A JP 3527466 B2 JP3527466 B2 JP 3527466B2
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JP
Japan
Prior art keywords
tank
deep
water
treatment plant
water treatment
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
Application number
JP2000249517A
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Japanese (ja)
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JP2002059195A (en
Inventor
善吉 安孫子
Original Assignee
善吉 安孫子
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Filing date
Publication date
Application filed by 善吉 安孫子 filed Critical 善吉 安孫子
Priority to JP2000249517A priority Critical patent/JP3527466B2/en
Publication of JP2002059195A publication Critical patent/JP2002059195A/en
Application granted granted Critical
Publication of JP3527466B2 publication Critical patent/JP3527466B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】この発明は、水深200m以
下の海水を採取して得られる海洋深層水の水処理プラン
トに関する。 【0002】 【従来の技術】水深200m以上の海水である海洋深層
水は、汚染が少なく海洋性細菌も少なく清浄性があると
共に、太陽光が届かないため海草が光合成せず、植物の
成長に必要な窒素やケイ酸などの栄養素を多く含むほ
か、ミネラルのバランスが良いので、この深層水を採取
して飲料水、発酵食品などの食品とか、医薬品、化粧品
などの医療・健康とか、養殖、土壌改良などの農・水産
業などの広い分野で利用されている。 【0003】 【発明が解決しようとする課題】しかしながら、従来の
海洋深層水の処理システムは、比較的コンパクトで量産
性に欠け、したがって生産コストが高価であり、最終製
品のコストを仲々下げることができないという不都合が
あった。 【0004】この発明は、海洋深層水の多量処理を可能
とし、安価で安全性の高い海洋深層水の水処理プラント
を提供することを目的とする。 【0005】 【課題を解決するための手段】この発明は以下の構成を
備えることにより、前記課題を解決することができる。 【0006】(1)水深200m以上の深さの海洋深層
水を採取できる1以上の深層水採取管、この採取管と接
続され揚水ポンプを介して設けられる1以上の深層水貯
溜タンク、之等貯溜タンクと順次と接続される粗濾過
槽、脱塩槽、膜分離モジュール槽、オゾン殺菌槽および
活性炭濾過槽を配設すると共に、前記深層水貯溜タンク
は、内部に回転する撹拌用羽根を縦設して成ることを特
徴とする海洋深層水の水処理プラント。 【0007】 【0008】 【発明の実施の形態】以下に、この発明の実施の形態を
説明する。 【0009】図1は、この発明に係る海洋深層水の水処
理プラントの一実施例を示す全体の外観図である。 【0010】1は、海洋2の水深200m以上に開口端
を開口させた深層水採取管を示し、図示では2本を並列
してあるが多数本配設できる。3は前記深層水採取管1
と接続し、次段の1以上配設される深層水貯溜タンク4
と接続される揚水ポンプ5を設置した建物を示し、揚水
ポンプ5の作用で海洋2の水深200m以上の海洋深層
水を採取し貯溜できるようになっている。図示では、揚
水ポンプ5から200トン級の大きさの3個の深層水貯
溜タンク4への配管6が各タンク4の下部に順次と接続
させてあるが、各タンク4へは上部に接続させて流下供
給するようにしても良い(図示せず)。7は各タンク4
内に配設した撹拌用羽根で、タンク4内で貯溜した海洋
深層水を常時または必要に応じて撹拌し、含有成分の均
一性を図っている。 【0011】そして、前記した揚水ポンプ5は電気制御
機構を伴うので、有蓋の建物3内に設置するのが好まし
い。また、他の複数の深層水貯溜タンク4は、海洋2に
近い場所が好ましいが、海洋2から離れた場所でも整地
された屋外のスペースに直接無蓋状態で設置して差支え
ない。 【0012】8は、前記貯溜タンク4と接続される粗濾
過槽を示し、海洋深層水中に含まれる不純物、ゴミなど
を、内蔵した各種フィルタを通過させて除去できるよう
になっている。9は、前記粗濾過槽8と接続される脱塩
槽を示し、逆浸透膜(REVERSE OSMOSI
S)により海洋深層水中の塩分や人体に有害な微生物な
どを排除し、純水を得ることができるものである。10
は次段の膜分離モジュール槽で、さらに微細な塵埃、臭
気、汚物などを除去できる。 【0013】11は、引続いて接続されるオゾン接触槽
を示し、純水化された深層水にオゾンガスを吹き付け殺
菌処理を行うと共に、最終段階の活性炭濾過槽12に送
給し、水処理された深層水中の不純物を吸着して、最終
処理された深層水を得る。 【0014】なお、前記した粗濾過槽8、脱塩槽9、膜
分離モジュール槽10、オゾン接触槽11並びに活性炭
濾過槽12は、一連の連続した装置としてプラットホー
ム13上に並設するものであるが、その配列は自由であ
るので並び変えることができる。 【0015】14はその他の配管、15はローリー車を
示し、前記プラットホーム13に隣接した車寄せ16に
導き、ここで最終段の活性炭濾過槽12を経て得られる
純水化した深層水を必要な配管14の給出口17より前
記ローリー車15のタンク内に供給出荷できるものであ
る。 【0016】18はプラットホーム13上に設けた前記
した各装置の上部を支持するフレーム、19は階段20
を利用して作業員が乗降して各装置をチェックするため
に歩行できるデッキを示す。 【0017】21は、前記タンク4の外壁に沿って配設
した螺旋階段、22は各タンク4の上蓋中心に設けた撹
拌用羽根7を回転させるためのモータを示す。 【0018】なお、図示していないが、前記プラットホ
ーム13上に設けられる粗濾過槽8には、給出コックを
設け、生け簀用の海水とか水族館などの海水として販売
提供できると共に、脱塩槽9には、除去される塩分副成
物を取り出すための装置を設け、抽出される塩分副成物
を各種塩の原料として販売提供できる。 【0019】叙上の構成より成るので、水深200m以
下の海洋深層水は、揚水ポンプ5により常時地上の深層
水貯溜タンク4に供給貯溜され保存できると共に、貯溜
中は撹拌用羽根7の回転でタンク4内で不純物などの固
形成分が沈下堆積することを防止して、深層水貯溜タン
ク4内を著しく汚染させる不都合はなく、次段の処理工
程へ未処理状態で供給できる。 【0020】次に、粗濾過槽8において、まず不純物、
ゴミなど、比較的粒径の大きな固形物を各種フィルタに
よって機械的に除去することができる。次に、脱塩槽9
に供給し、ここで例えば逆浸透膜の働きにより、海水よ
り純水に変換して飲用可能とすることができる。この状
態で飲用可能な純水となるが、さらに菌などが含まれて
いるので、引続きオゾン接触槽11に導き殺菌処理を行
うと共に、活性炭濾過槽12に移行させて、脱臭、脱色
などの最終処理を行って、製品とする淡水化された海洋
深層水を得ることができる。 【0021】 【発明の効果】この発明によれば、全体がシステム化さ
れ、かつユニット化できるので、200m以上の海洋深
層水を採取できる海に臨まれた海岸の未利用土地を活用
することにより、コスト的にも極めて安価に提供でき、
得られる淡水化されミネラル分や栄養価の高い深層水
は、飲用はもとより、各種用途に安価に提供できる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deep ocean water treatment plant obtained by collecting seawater having a depth of 200 m or less. 2. Description of the Related Art Deep sea water, which is a seawater at a depth of 200 m or more, has low pollution and little marine bacteria and is clean. It contains a lot of necessary nutrients such as nitrogen and silicic acid, and has a good mineral balance, so this deep water is collected and used for foods such as drinking water and fermented foods, medical and health products such as pharmaceuticals and cosmetics, aquaculture, It is used in a wide range of fields such as agriculture and fisheries such as soil improvement. [0003] However, conventional deep sea water treatment systems are relatively compact and lack mass production, and are therefore expensive to produce, and can reduce the cost of the final product. There was an inconvenience of not being able to do so. [0004] It is an object of the present invention to provide an inexpensive and highly safe deep-sea water treatment plant that enables a large amount of deep-sea water treatment. [0005] The present invention can solve the above-mentioned problems by providing the following structure. (1) One or more deep water sampling pipes capable of sampling deep sea water having a depth of 200 m or more, one or more deep water storage tanks connected to the sampling pipes and provided through a pumping pump, etc. A coarse filtration tank, a desalination tank, a membrane separation module tank, an ozone sterilization tank, and an activated carbon filtration tank which are sequentially connected to the storage tank are provided, and the deep water storage tank is provided.
Is a deep-sea water treatment plant characterized by vertically rotating stirring blades inside . [0008] Embodiments of the present invention will be described below. FIG. 1 is an overall external view showing one embodiment of a deep-sea water treatment plant according to the present invention. Reference numeral 1 denotes a deep water sampling pipe having an open end opened at a depth of 200 m or more in the ocean 2, and two pipes are arranged in parallel in FIG. 3 is the deep water sampling pipe 1
And the deep water storage tank 4 provided at least one of the following stages
1 shows a building provided with a pump 5 connected to the ocean, and the deep pump water of the ocean 2 having a depth of 200 m or more can be collected and stored by the action of the pump 5. In the drawing, the pipes 6 from the pump 5 to the three deep water storage tanks 4 of 200 ton class are sequentially connected to the lower part of each tank 4, but the upper part is connected to each tank 4. Alternatively, it may be supplied downstream (not shown). 7 is each tank 4
The deep sea water stored in the tank 4 is constantly or as required stirred by the stirring blades disposed therein, thereby achieving uniformity of the contained components. Since the above-mentioned pump 5 has an electric control mechanism, it is preferable to install the pump 5 in the covered building 3. The other plurality of deep water storage tanks 4 are preferably located close to the ocean 2, but may be installed directly without cover in a leveled outdoor space even at a place away from the ocean 2. Reference numeral 8 denotes a coarse filtration tank connected to the storage tank 4 so that impurities, dust and the like contained in deep sea water can be removed by passing through various built-in filters. Reference numeral 9 denotes a desalination tank connected to the coarse filtration tank 8, and a reverse osmosis membrane (REVERSE OSMOSI).
According to S), pure water can be obtained by eliminating salts in the deep sea water and microorganisms harmful to the human body. 10
Is the next stage of the membrane separation module tank, which can remove finer dust, odor and dirt. Reference numeral 11 denotes an ozone contact tank which is continuously connected. The ozone contact tank is sprayed with ozone gas to the purified deep water to perform a sterilization treatment, and is supplied to an activated carbon filtration tank 12 at the final stage to be treated with water. Absorb the impurities in the deep water to obtain the final treated deep water. The coarse filtration tank 8, the desalination tank 9, the membrane separation module tank 10, the ozone contact tank 11 and the activated carbon filtration tank 12 are arranged side by side on a platform 13 as a series of continuous devices. However, the arrangement is free and can be rearranged. Reference numeral 14 denotes other piping, and reference numeral 15 denotes a lorry vehicle. The truck is guided to a carriage 16 adjacent to the platform 13, where the purified water obtained through the activated carbon filtration tank 12 at the final stage is supplied with necessary piping. It can be supplied and shipped into the tank of the lorry 15 from the supply port 17 of 14. Reference numeral 18 denotes a frame that supports the upper portion of each of the above-mentioned devices provided on the platform 13, and 19 denotes a staircase 20.
1 shows a deck on which a worker can get on and off and walk to check each device. Reference numeral 21 denotes a spiral staircase disposed along the outer wall of the tank 4, and reference numeral 22 denotes a motor for rotating the stirring blades 7 provided at the center of the upper lid of each tank 4. Although not shown, the coarse filtration tank 8 provided on the platform 13 is provided with a supply cock so that it can be sold and supplied as seawater for living cages or seawater such as an aquarium. Is provided with a device for removing the salt by-product to be removed, and the salt by-product to be extracted can be sold and provided as a raw material for various salts. With the above construction, the deep sea water having a depth of 200 m or less can be constantly stored and stored in the deep water storage tank 4 on the ground by the pump 5 while the stirring blade 7 rotates during the storage. Preventing solid components such as impurities from settling and depositing in the tank 4, there is no inconvenience of significantly contaminating the deep water storage tank 4, and it can be supplied to the next processing step in an unprocessed state. Next, in the coarse filtration tank 8, impurities,
Solid matter having a relatively large particle size such as dust can be mechanically removed by various filters. Next, desalination tank 9
, Where, for example, by the action of a reverse osmosis membrane, seawater can be converted into pure water and made drinkable. In this state, it becomes pure water that can be drunk, but further contains bacteria and the like, so that it is continuously led to the ozone contact tank 11 for sterilization treatment, and is transferred to the activated carbon filtration tank 12 for final deodorization and decolorization. By performing the treatment, desalinated deep sea water can be obtained as a product. According to the present invention, since the entire system can be systemized and unitized, the unused land of the coast facing the sea from which deep seawater of 200 m or more can be collected can be utilized. , Can be provided at very low cost,
The resulting desalinated mineral water and nutrient-rich deep water can be inexpensively provided for various uses as well as for drinking.

【図面の簡単な説明】 【図1】 この発明に係る海洋深層水の水処理プラント
の一例を示す全体の外観図 【図2】 図1に示す水処理プラントのフローチャート 【符号の説明】 1 深層水採取管 4 深層水貯溜タンク 5 揚水ポンプ 8 粗濾過槽 9 脱塩槽 10 膜分離モジュール槽 11 オゾン接触槽 12 活性炭濾過槽 15 ローリー車
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an overall external view showing an example of a deep-sea water treatment plant according to the present invention. FIG. 2 is a flowchart of the water treatment plant shown in FIG. Water sampling pipe 4 Deep water storage tank 5 Pumping pump 8 Rough filtration tank 9 Desalination tank 10 Membrane separation module tank 11 Ozone contact tank 12 Activated carbon filtration tank 15 Truck

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C02F 9/00 C02F 9/00 502R 503 503A B01D 61/02 500 B01D 61/02 500 C02F 1/28 C02F 1/28 F 1/44 1/44 G 1/50 510 1/50 510A 520 520F 531 531R 540 540A 550 550H 560 560B 560E 560Z 1/78 1/78 // A23L 2/00 A23L 2/00 V (56)参考文献 特開 平11−207394(JP,A) 特開 平9−290260(JP,A) 特開 平11−207392(JP,A) 特開 平6−254553(JP,A) 特開2000−87579(JP,A) 特開2000−159655(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 61/02 C02F 1/00 - 9/00 A23L 2/00 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification code FI C02F 9/00 C02F 9/00 502R 503 503A B01D 61/02 500 B01D 61/02 500 C02F 1/28 C02F 1/28 F 1 / 44 1/44 G 1/50 510 1/50 510A 520 520F 531 531R 540 540A 550 550H 560 560B 560E 560Z 1/78 1/78 // A23L 2/00 A23L 2/00 V (56) Reference JP-A-9-290260 (JP, A) JP-A-11-207392 (JP, A) JP-A-6-254553 (JP, A) JP-A-2000-87579 (JP, A) JP-A-2000-159655 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B01D 61/02 C02F 1/00-9/00 A23L 2/00

Claims (1)

(57)【特許請求の範囲】 【請求項1】 水深200m以上の深さの海洋深層水を
採取できる1以上の深層水採取管、この採取管と接続さ
れ揚水ポンプを介して設けられる1以上の深層水貯溜タ
ンク、之等貯溜タンクと順次と接続される粗濾過槽、脱
塩槽、膜分離モジュール槽、オゾン殺菌槽および活性炭
濾過槽を配設すると共に、前記深層水貯溜タンクは、内
部に回転する撹拌用羽根を縦設して成ることを特徴とす
る海洋深層水の水処理プラント。
(57) [Claims 1] One or more deep water sampling pipes capable of collecting deep ocean water having a depth of 200m or more, and one or more provided through a pump connected to the sampling pipes. A deep water storage tank, a coarse filtration tank, a desalination tank, a membrane separation module tank, an ozone sterilization tank, and an activated carbon filtration tank, which are sequentially connected to the deep water storage tank, are provided.
A deep-sea water treatment plant characterized by vertically rotating rotating stirring blades in a section .
JP2000249517A 2000-08-21 2000-08-21 Deep ocean water treatment plant Expired - Fee Related JP3527466B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000249517A JP3527466B2 (en) 2000-08-21 2000-08-21 Deep ocean water treatment plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000249517A JP3527466B2 (en) 2000-08-21 2000-08-21 Deep ocean water treatment plant

Publications (2)

Publication Number Publication Date
JP2002059195A JP2002059195A (en) 2002-02-26
JP3527466B2 true JP3527466B2 (en) 2004-05-17

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Country Link
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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100946158B1 (en) 2007-09-07 2010-03-11 서희동 A storage equipment of the deep sea water
JP2009297685A (en) * 2008-06-17 2009-12-24 Nyk Kk Method and apparatus for producing fresh water

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06254553A (en) * 1993-03-08 1994-09-13 Shinko Electric Co Ltd Apparatus for producing pure water
JP2887105B2 (en) * 1996-04-24 1999-04-26 幸子 林 Method and apparatus for producing drinking water and salt
JP4073072B2 (en) * 1998-01-26 2008-04-09 Agcエンジニアリング株式会社 Raw water desalination method and desalination equipment by membrane method
JPH11207392A (en) * 1998-01-28 1999-08-03 Zoom:Kk Water purifying treatment device
JP2000087579A (en) * 1998-09-11 2000-03-28 Toshiba Corp Multi-purpose use plant for deep layer water in ocean
JP2000159655A (en) * 1998-11-24 2000-06-13 Kochi Prefecture Cosmetic

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