JP2003225639A - Method for treating jellyfishes getting mixed into sea water intake line - Google Patents

Method for treating jellyfishes getting mixed into sea water intake line

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Publication number
JP2003225639A
JP2003225639A JP2002030306A JP2002030306A JP2003225639A JP 2003225639 A JP2003225639 A JP 2003225639A JP 2002030306 A JP2002030306 A JP 2002030306A JP 2002030306 A JP2002030306 A JP 2002030306A JP 2003225639 A JP2003225639 A JP 2003225639A
Authority
JP
Japan
Prior art keywords
jellyfish
intake line
treating
mixed
liquefied
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.)
Pending
Application number
JP2002030306A
Other languages
Japanese (ja)
Inventor
Koji Hayashida
耕治 林田
Norio Matsuki
徳生 松木
Yoshikatsu Kijima
佳克 木島
Tadakazu Hashikawa
忠和 橋川
Takashi Sakamoto
隆志 坂元
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.)
Electric Power Development Co Ltd
Original Assignee
Electric Power Development 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 Electric Power Development Co Ltd filed Critical Electric Power Development Co Ltd
Priority to JP2002030306A priority Critical patent/JP2003225639A/en
Publication of JP2003225639A publication Critical patent/JP2003225639A/en
Pending legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for treating the mixed jellyfishes entering sea water intake line with which solid waste disposal quantity is reduced, treatment is easy and cost is reduced. <P>SOLUTION: In this method for treating the mixed jellyfishes which flow and enter when sea water is taken as industrial coolant, jellyfishes and fishery product are landed and separated from the seawater intake line by using a draining net conveyor, etc., and the separated jellyfishes and fishery product are transferred to a tank and are stored for several days in a tight closure state of air interruption. Therein, after confirming that the jellyfishes are naturally dissolved and liquefied by anaerobic decomposition, the liquefied matter is separated and then is subjected to deodorization treatment by a deodorizer. <P>COPYRIGHT: (C)2003,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、工業用冷却水とし
ての海水取水ラインへの混入クラゲの処理方法に関し、
特に水揚げされる混入クラゲの全量を液状化し脱臭処理
することで固形廃棄物としての減容化とその処理費用の
低減を図る海水取水ラインへの混入クラゲ類の処理方法
に関するものである。
TECHNICAL FIELD The present invention relates to a method for treating jellyfish mixed in a seawater intake line as industrial cooling water,
In particular, the present invention relates to a method for treating jellyfish that is mixed in a seawater intake line to liquefy and deodorize all of the jellyfish that are landed to reduce the volume as solid waste and reduce the treatment cost.

【0002】[0002]

【従来の技術】海岸に近い火力発電所の復水器や、化学
装置産業等の大型熱交換器には、大量の冷却水を必要と
することから、海水を工業用冷却水として使用する機会
が多い。しかし、かかる工業用冷却水としての海水取水
ラインには、クラゲや魚介類の異物が流入し易く、ポン
プ・配管や伝熱管等を閉塞したり、伝熱管壁に付着して
伝熱効率を悪化させる要因となることから、これらの混
入を極力防止する必要がある。クラゲの種類としては、
水クラゲ(傘の直径が1cm〜30cm、ごく稀に1m
に達し、捕集クラゲの大部分を占める)、アカクラゲ
(傘の直径が9cm〜12cm、大きいもので50cm
程度が捕集され、触手には強毒がある。)、カブトクラ
ゲ(卵型・小型で大きいものでも10cm程度の透明で
ゼリー状。クラゲ防止ネットを簡単に通過)等が知られ
ている。
2. Description of the Related Art Since a large amount of cooling water is required for condensers of thermal power plants near the coast and large heat exchangers in the chemical equipment industry, there is an opportunity to use seawater as industrial cooling water. There are many. However, foreign substances such as jellyfish and seafood easily flow into the seawater intake line as industrial cooling water, and block pumps, pipes, heat transfer pipes, etc., or adhere to the heat transfer pipe wall to deteriorate heat transfer efficiency. It is necessary to prevent these from being mixed in as much as possible. As for the type of jellyfish,
Water jellyfish (Umbrella diameter 1 cm to 30 cm, very rarely 1 m
And the majority of collected jellyfish), red jellyfish (umbrella diameter 9cm-12cm, large one 50cm)
The degree is collected and the tentacles are highly poisonous. ), Horseshoe jellyfish (egg-shaped, small and large, transparent and jelly-like with a size of about 10 cm. It easily passes through a jellyfish prevention net).

【0003】かかるクラゲ類は特に6月中旬〜8月下旬
までの間、大量に発生して海水取水ラインヘ流入する量
も多くなる。例えば火力発電所における復水器用冷却水
として使用される海水取水ラインには、通常、先端部に
クラゲ流入防止網(約75mm□)が設置され、更に途
中の取水ピットへの流入ラインには、複数のレーキバー
スクリーンやロータリースクリーン等が設置されてお
り、これでクラゲや魚介類を固形塵芥物として順次海水
から掻き揚げて塵芥排出ラインヘ移し、洗浄水とともに
ネットの仕切り堰で複数に区画されたトラッシュピツト
(廃棄物ピット)へ流し込む。ここでトラッシュピツト
に堆積したクラゲや魚介類は固形廃棄物としてバキュウ
ム車等に吸い上げたり、人手により掻きだしたりして搬
出し産業系一般廃棄物として処理されると共に、残りの
洗浄水は海水取水ラインへ戻されている。
From the middle of June to the end of August, a large amount of such jellyfish is generated and the amount of the jellyfish flowing into the seawater intake line is also large. For example, a seawater intake line used as condenser cooling water in a thermal power plant is usually equipped with a jellyfish inflow prevention network (about 75 mm □) at its tip, and further along the inflow line to the intake pit on the way, Multiple rake bar screens, rotary screens, etc. are installed, and with this, jellyfish and seafood are sequentially scraped off from seawater as solid dust and transferred to the dust discharge line. Pour into trash pit (waste pit). The jellyfish and seafood accumulated on the trash pits are sucked up into a vacuum truck etc. as solid waste, or they are scraped out manually and carried out to be treated as industrial general waste, while the remaining washing water is seawater. Returned to the intake line.

【0004】[0004]

【発明が解決しようとする課題】かかる固形廃棄物の産
業系一般廃棄物としての処理方法としては、埋立て・焼
却及び発酵等による処理が一般的であるが、クラゲの成
分は水分が約95%、たんぱく質等の有機物が約5%か
らなり、しかも多量の海水が混入しているので、引き取
りも困難な状況であり処理コストが高くなる。従って、
クラゲ類の処理量をより減容化させて処理コストを低減
化する対策が強く望まれている。本発明はかかる現状に
鑑みて、海水取水ラインに流入する混入クラゲ等の固形
廃棄物としての減容化とその処理費用の低減を図る処理
方法を提供することを課題とする。
As a method of treating such solid waste as industrial general waste, landfilling, incineration, fermentation and the like are generally used, but the water content of the jellyfish component is about 95. %, Organic matter such as protein is about 5%, and since a large amount of seawater is mixed, it is difficult to collect and the processing cost becomes high. Therefore,
It is strongly desired to take measures to further reduce the treatment amount of jellyfish and reduce the treatment cost. In view of the present situation, an object of the present invention is to provide a treatment method for reducing the volume of solid waste such as mixed jellyfish flowing into a seawater intake line and reducing the treatment cost.

【0005】[0005]

【課題を解決するための手段】本発明者等は、上記課題
について種々検討した結果、クラゲはポリタンク等に空
気遮断の密閉状態で数日間貯留するだけで容易に嫌気性
分解して液状化し固形物は減容化するという新事実に着
眼し本発明を完成した。即ち本発明は、海水を工業用冷
却水として取水する際に流入する混入クラゲ類の処理方
法であって、海水取水ラインからクラゲや魚介類等の固
形物を水切りネットコンベヤ等で水揚げ分離し、分離し
たクラゲ類をタンクに移し空気遮断の密閉状態で数日の
間貯留しておき、クラゲが嫌気性分解により自然溶解し
液状化したことを確認してから液状化物を分離し、該液
状化物を消臭薬剤で脱臭処理することを特徴とする海水
取水ラインへの混入クラゲ類の処理方法である。
Means for Solving the Problems As a result of various studies on the above problems, the present inventors have found that jellyfish can be easily anaerobically decomposed into a liquefied solid by simply storing it in a plastic tank or the like for several days in an airtight closed state. The present invention has been completed by focusing on the new fact that the volume of an article is reduced. That is, the present invention is a method of treating mixed jellyfish that flows in when seawater is taken in as industrial cooling water, wherein solids such as jellyfish and seafood from the seawater intake line are landed and separated by a draining net conveyor or the like, The separated jellyfish are transferred to a tank and stored for several days in an air-tight closed state, and after confirming that the jellyfish spontaneously dissolved and liquefied by anaerobic decomposition, the liquefact is separated and Is a method for treating jellyfish mixed in a seawater intake line, which is characterized in that the deodorant is treated with a deodorant agent.

【0006】また、上記本発明において、消臭薬剤で脱
臭処理した液状化物は、活性汚泥設備等で無害化処理す
ると共に、タンクから液状化物を分離した後の減容化し
た残留固形物は一般固形廃棄物として処理する混入クラ
ゲ類の処理方法である。さらに、上記本発明において、
液状化物の脱臭処理は、循環タンク内で液状化物に消臭
薬剤を添加しポンプで循環処理することが設備コスト面
で望ましい。さらに上記本発明において、消臭薬剤とし
ては、次亜塩素酸ソーダを使用することが脱臭効果と処
理コスト面で最も望ましい。
Further, in the present invention, the liquefied material deodorized with a deodorant agent is detoxified in an activated sludge facility or the like, and the volume-reduced residual solid matter after the liquefied material is separated from the tank is generally This is a method for treating mixed jellyfish that is treated as solid waste. Furthermore, in the above-mentioned present invention,
For deodorizing liquefaction, it is desirable in terms of equipment cost to add a deodorant agent to the liquefaction in a circulation tank and circulate with a pump. Further, in the above-mentioned present invention, it is most desirable to use sodium hypochlorite as a deodorizing agent in terms of deodorizing effect and processing cost.

【0007】[0007]

【発明の実施の形態】以下、本発明の実施の形態につい
て添付図に従って詳細に説明する。図1は、海水取水ラ
インを示す概略断面図である。図2は、トラッシュピツ
ト構造を示す概略斜視図である。図3は、クラゲ処理状
況を示す概略の全体作業フロー図である。先ず図1にお
いて、深層の海水取水用ライン1の最先端にはクラゲ流
入防止網(75mm□)2が設置され、更に陸上部の取
水ピットへの流入ライン3の途中には、複数のレーキバ
ースクリーン4やロータリースクリーン5等が設置され
ている。これらスクリーンでクラゲや魚介類等の固形塵
芥物を海水より掻き揚げて、図示していない塵芥排出ラ
インヘ移して除かれる。固形塵芥物が除かれた海水は取
水ピット6に貯留され、ここに設置された循環水ポンプ
7で復水器等の工業用冷却水として循環送水される。な
お取水ピットには上記した塵芥排出ラインへのスクリー
ン洗浄用ポンプ8も設置されている。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below with reference to the accompanying drawings. FIG. 1 is a schematic sectional view showing a seawater intake line. FIG. 2 is a schematic perspective view showing the trash pit structure. FIG. 3 is a schematic overall work flow diagram showing a jellyfish processing situation. First, in FIG. 1, a jellyfish inflow prevention network (75 mm □) 2 is installed at the extreme end of the deep seawater intake line 1, and a plurality of rake bars are provided in the middle of the inflow line 3 to the intake pit on the land. A screen 4, a rotary screen 5, etc. are installed. With these screens, solid waste such as jellyfish and seafood is scraped from seawater and transferred to a dust discharge line (not shown) for removal. The seawater from which solid dust has been removed is stored in the intake pit 6, and is circulated by the circulating water pump 7 installed therein as industrial cooling water for a condenser or the like. In addition, the screen cleaning pump 8 for the dust discharge line is also installed in the water intake pit.

【0008】上記したクラゲや魚介類等の固形塵芥物
は、レーキバースクリーン4とロータリースクリーン5
等で掻き揚げられた後で、スクリーン裏面からスクリー
ン洗浄ポンプ8からの洗浄水の注水で塵芥排出ライン9
(図2参照)へ落とされ流下しつつ、トラッシュピツト
(廃棄物ピット)10ヘ排出される。ここでトラッシュピ
ツト10は、通常は図2に示すように、ネット製の仕切
り堰11でA,B,C槽等に仕切られており、それぞれ
の槽で固形塵芥物は堆積され、C槽出口の配管ライン1
2からは固形塵芥物を除かれた洗浄水だけが前記した取
水ピットへ循環される。A,B,C槽に堆積された固形
塵芥物はそれぞれの槽から水切りネットコンベヤ等で水
揚げ分離してもよいが、より好ましくは塵芥排出ライン
からトラッシュピツトへの流入口付近に、水切りネット
コンベヤー13を設置して、ここで固形塵芥物を該ネッ
トコンベヤーの駆動で連続的に洗浄水面上から掻き揚げ
て水切りしつつ分離することが好ましい。
The solid dust particles such as jellyfish and seafood mentioned above are rake bar screen 4 and rotary screen 5.
After being scooped up by a cleaning machine, etc., by injecting washing water from the screen washing pump 8 from the back side of the screen, the dust discharging line 9
(See Fig. 2) While falling and flowing down, the trash pit
(Waste pit) It is discharged to 10. As shown in FIG. 2, the trash pit 10 is normally divided into A, B, and C tanks by a net-made partition weir 11, and solid dust is accumulated in each tank, and the C tank is Outlet piping line 1
From 2, only the washing water from which solid dust is removed is circulated to the intake pit described above. The solid wastes accumulated in the tanks A, B and C may be separated from the respective tanks by landing with a draining net conveyor or the like, but more preferably, a draining net is provided near the inlet from the dust discharging line to the trash pit. It is preferable to install a conveyor 13 where the solid waste is continuously scraped off the surface of the washing water by driving the net conveyor to separate it while draining water.

【0009】本発明においては、このようにして水切り
で分離された固形塵芥物14はトラッシュピツト外の容
器15に一時集められ、図3に示すように適宜真空ポン
プ16等を利用してポリ容器等の密閉タンク17へ充填
される。そしてポリ容器等の密閉タンク17に充填され
たクラゲは、空気遮断の密閉状態で数日間貯留すること
に最大の特徴を有する。ここでクラゲは、約2m3のポ
リ容器等に容量の95%程度充填して空気遮断の嫌気性
状態で放置した場合、嫌気性分解が進行して約3日間程
度で完全に自然溶解し液状化することが確かめられてい
る。従って嫌気性状態で放置する日数はポリ容器の容量
や充填量にもよるが、通常2〜5日間、好ましくは3日
間程度であれば良い。
In the present invention, the solid waste material 14 thus separated by draining is temporarily collected in a container 15 outside the trash pit and, as shown in FIG. It is filled in a closed tank 17 such as a container. The jellyfish filled in a closed tank 17 such as a plastic container has the greatest feature in storing for several days in an air-tight closed state. Here, when jellyfish are filled in a plastic container of about 2 m 3 at about 95% of the capacity and left in an anaerobic state with air blocking, anaerobic decomposition progresses and completely dissolves naturally in about 3 days. It is confirmed that it will change. Therefore, the number of days to be left in the anaerobic state depends on the capacity and filling amount of the plastic container, but it is usually 2 to 5 days, preferably about 3 days.

【0010】クラゲの処理量が多い場合には、密閉タン
ク17の容積を大きくしたり、複数個配列しておき、順
次、経過日数ごとに充填する容器を替えながら連続的に
処理できるようにすることが望ましい。次いで、クラゲ
がかかる嫌気性分解により自然溶解し液状化したことを
確認して、液状化物18をバキュウームカー19等へ吸
い上げて残留固形物20から分離した後、液状化物処理
設備へ移送して、そこで該液状化物を脱臭処理して無害
化する。特に、クラゲの嫌気性分解で液状化した中に
は、主に硫化水素やメチルメルカプタン等の硫黄化合物
が悪臭物として含まれており、これを消臭薬剤で脱臭処
理する必要がある。
When the amount of jellyfish to be processed is large, the volume of the closed tank 17 may be increased or a plurality of jellyfish may be arranged so that the jellyfish can be continuously processed while changing the container to be filled according to the elapsed days. Is desirable. Next, after confirming that the jellyfish were naturally dissolved and liquefied by such anaerobic decomposition, the liquefied material 18 was sucked up into a vacuum chamber car 19 or the like and separated from the residual solid matter 20, and then transferred to a liquefied material treatment facility. At this point, the liquefied product is deodorized to render it harmless. In particular, liquefied anaerobically decomposed jellyfish mainly contains sulfur compounds such as hydrogen sulfide and methyl mercaptan as malodorous substances, which need to be deodorized with a deodorant agent.

【0011】本発明のクラゲの液状化物の脱臭処理設備
としては、約50m3の貯留タンク21内に液状化物を
投入し、それに消臭薬剤22を添加してポンプ23で循
環処理する方式が脱臭効果とCOD低減効果も得られる
ことから、簡便で設備コスト的にも安価で有利である。
また消臭薬剤22としては、酸化作用のある次亜塩素酸
ナトリウムが脱臭効果に優れ、且つ安価である点で最も
好ましいが、その他に市販品として例えば、硝酸塩を主
成分とした消臭剤であるステンチカットNX-500、クリレ
イザーN-350(以上栗田工業製)、二酸化塩素を主成分
とした消臭剤であるタイスライムDC(タイホー工業製)
等が使用できる。なお、かかる酸化作用のある消臭薬剤
にはクラゲの溶解性は殆どなく、特に消臭薬剤を添加し
た後に液状化していないクラゲを再投入した場合には、
クラゲは液化しなくなることから、貯留タンク22内に
クラゲを再投入することは望ましくない。
As the deodorizing equipment for liquefying jellyfish liquefaction of the present invention, a method in which the liquefying agent is put into a storage tank 21 of about 50 m 3 and a deodorant agent 22 is added to the liquefying agent to circulate it by a pump 23 Since the effect and the COD reduction effect can be obtained, it is advantageous because it is simple and the equipment cost is low.
Further, as the deodorizing agent 22, sodium hypochlorite having an oxidizing action is most preferable in that it has an excellent deodorizing effect and is inexpensive, but as a commercially available product, for example, a deodorizing agent mainly containing nitrate is Stenchi Cut NX-500, Clearizer N-350 (made by Kurita Kogyo), and Thai slime DC (made by Taiho Kogyo) which is a deodorant mainly containing chlorine dioxide.
Etc. can be used. In addition, the deodorant having such an oxidizing action has almost no solubility of jellyfish, and in particular, when the liquefied jellyfish is re-introduced after adding the deodorant,
It is not desirable to re-introduce the jellyfish into the storage tank 22 because the jellyfish will not liquefy.

【0012】本発明においては、上述の貯留タンク22
内に液状化物18と消臭薬剤22を添加してポンプ23
で循環処理しつつ脱臭処理した液状化物は、脱臭効果と
ある程度までのCOD低減効果を確認して後は、適宜、
通常の既存設備である活性汚泥設備24等で処理するこ
とでCOD濃度がMAX10ppm、平均7ppmの状
態で放流処理することができる。この場合、貯留タンク
22内への液状化物は連続的に投入し、脱臭とCOD低
減を監視しつつ連続的に抜き出しを行なうことが望まし
い。また、25は必要に応じて使用する構内排水ピット
である。なお本発明においては、密閉タンク17から液
状化物を分離した後の減容化した残留固形物20は、従
来のように一般固形廃棄物として埋立て・焼却処理する
が、その処理量は僅かであり処理頻度も大幅に低下す
る。
In the present invention, the storage tank 22 described above is used.
Pump 23 by adding liquefied substance 18 and deodorant agent 22
After confirming the deodorizing effect and the COD reducing effect up to a certain degree, the liquefied material that has been deodorized while being circulated by
By treating the activated sludge facility 24, which is a normal existing facility, the COD concentration can be discharged at a maximum concentration of 10 ppm and an average of 7 ppm. In this case, it is desirable that the liquefied material is continuously charged into the storage tank 22 and continuously withdrawn while monitoring deodorization and COD reduction. Reference numeral 25 is a drainage pit in the premises which is used as necessary. In the present invention, the volume-reduced residual solid matter 20 after separating the liquefied material from the closed tank 17 is landfilled and incinerated as general solid waste as in the conventional case, but the treatment amount is small. Yes Processing frequency is also significantly reduced.

【0013】[0013]

【作用】海水取水ラインから分離したクラゲ類をタンク
に移し空気遮断の密閉状態で貯留するだけでクラゲが嫌
気性分解により自然溶解し液状化することから、海水の
混入がない液状化物と減容化した残留固形物とに分離し
て、それぞれの形態に応じた最適な廃棄物処理作業を容
易に行なうことができる。即ち、液状化物は消臭薬剤と
共に貯留タンクで配管ラインによるポンプ循環するだけ
で脱臭処理が極めて安価に処理できるとともに、既存設
備である活性汚泥設備等で処理することでCOD濃度を
規定値以下の状態で放流処理することができる。また固
形廃棄物は大幅に減容化されていることからその処理頻
度が大幅に減少する等の作用効果が得られる。
[Function] Just by transferring the jellyfish separated from the seawater intake line to a tank and storing them in an air-tight closed state, the jellyfish will spontaneously dissolve and liquefy due to anaerobic decomposition. It is possible to easily carry out the optimum waste treatment work according to each form by separating it into the solidified residual solid matter. That is, the liquefaction can be processed at a very low cost by simply circulating the liquid deodorant together with the deodorant in the storage tank with a pump through a piping line, and the COD concentration of the existing equipment such as activated sludge equipment can be kept below a specified value. It can be discharged in the state. Further, since the volume of solid waste is greatly reduced, it is possible to obtain operational effects such as a significant reduction in the treatment frequency.

【0014】[0014]

【実施例】次に本発明の実施例を説明する。 実施例1 海水取水ラインから水切りネットコンベヤで水揚げ分離
したクラゲ類を2m3のポリタンクに充填率約95%で
充填し、空気遮断の完全密閉状態で3日間貯留した結
果、クラゲは自然溶解し完全に液状化していることが確
かめられた。この液状化物の原液は、H2Sが約100
0ppmで悪臭を発生し、総合排水希釈処理でも処理が
不可であった。液状化物をラボ試験タンクに移して、各
種の消臭薬剤を添加し撹拌処理した結果、最も優れたも
のから最も劣るものまでを◎〜×の順位で表1に示す。
EXAMPLES Examples of the present invention will be described below. Example 1 Jellyfish that had been landed and separated from a seawater intake line on a draining net conveyor were filled in a 2 m 3 poly tank at a filling rate of about 95%, and stored for 3 days in a completely air-sealed state. It was confirmed that it was liquefied. This liquefied stock solution contains approximately 100 H 2 S.
A bad odor was generated at 0 ppm, and the treatment was impossible even with the comprehensive wastewater dilution treatment. The liquefied product was transferred to a laboratory test tank, various deodorant chemicals were added, and the mixture was stirred. As a result, the most excellent ones to the least inferior ones are shown in Table 1 in the order of ⊚ to ×.

【0015】[0015]

【表1】 消臭剤:ステンチカットNX-500(硝酸塩系消臭剤:栗
田工業製) 消臭剤:上記NX-500+クリレイザーN350(硝酸塩系消
臭剤:栗田工業製) 消臭剤:タイスライムDC(二酸化塩素系脱臭清浄剤:
タイホー工業製) 消臭剤:次亜塩素酸ナトリウム 処理コスト:消臭剤の処理コストコストを1としたと
きの概略倍数
[Table 1] Deodorant: Stenchicut NX-500 (nitrate-based deodorant: Kurita Kogyo) Deodorant: NX-500 + Clearase N350 (nitrate-based deodorant: Kurita Kogyo) Deodorant: Thai slime DC (dioxide) Chlorine deodorant cleaner:
Deodorant: Sodium hypochlorite treatment cost: Approximate multiple when deodorant treatment cost is 1.

【0016】表1の結果より、消臭薬剤添加量の消臭効
果の順位は、は1%、は0.2%で十分な効果
があることが確かめられた。消臭薬剤のクラゲの溶解性
は、≧>>、なおとは未溶解クラゲを添加
すると液化しない。 処理コストでは、>>>、 総合評価では、>>>、 以上から、いずれの消臭薬剤も消臭効果は認められるが
の次亜塩素酸ナトリウムがコスト面から最も優れてい
ることがわかる。
From the results shown in Table 1, it was confirmed that the order of deodorant effect of the deodorant drug addition amount was 1%, and 0.2% was sufficient. The solubility of jellyfish as a deodorant drug is ≧ >>, and it does not liquefy when undissolved jellyfish is added. From the above, it is clear that sodium hypochlorite is the most excellent in terms of cost, although the deodorizing effects of all deodorizing agents are recognized.

【0017】実施例2 実施例1で使用した2m3のポリタンクの複数個から、
それぞれ液状化物だけを20m3抜き出して、50m3
循環タンクに投入し、消臭薬剤として次亜塩素酸ナトリ
ウム1%相当を添加しポンプによる循環処理を行なっ
た。次亜塩素酸ナトリウム添加後15分間の循環処理に
よって、液状化物の初期COD濃度は270ppmから
147ppmに低下していることが確認された。また循
環処理による気液接触の酸化作用により臭気も減少し、
約48時間後には臭気のないことが確認できた。またC
OD濃度も緩やかに低下したが、その経過時間によるC
OD濃度変化を図4に示す。図4のCOD低下状況及び
臭気確認結果から、タンク循環処理は約72時間で40
ppmで平衡状態となることがわかった。次いでCOD
濃度40ppmの液状化物は、既存の総合排水処理装置
である活性汚泥設備にて処理し、所内管理値であるCO
D濃度MAX10ppm、平均7ppmの範囲内で放流
できた。
Example 2 From a plurality of 2 m 3 plastic tanks used in Example 1,
20 m 3 of each liquefied product was taken out, put into a circulation tank of 50 m 3 , and added with 1% of sodium hypochlorite as a deodorant, and circulated by a pump. It was confirmed that the initial COD concentration of the liquefied product was lowered from 270 ppm to 147 ppm by the circulation treatment for 15 minutes after the addition of sodium hypochlorite. In addition, the odor is reduced by the oxidation effect of gas-liquid contact due to the circulation treatment,
It was confirmed that there was no odor after about 48 hours. Also C
The OD concentration also decreased gradually, but C depending on the elapsed time
The change in OD concentration is shown in FIG. From the COD reduction situation and the odor confirmation result in Fig. 4, the tank circulation process took about 40 hours in about 72 hours.
It was found to be in equilibrium at ppm. Then COD
The liquefied substance with a concentration of 40 ppm is treated with activated sludge equipment, which is an existing integrated wastewater treatment device, and CO
The D concentration could be discharged within the range of MAX 10 ppm and average 7 ppm.

【0018】[0018]

【発明の効果】以上の結果から明らかなように本発明に
よれば、海水取水ラインから分離したクラゲ類をタンク
に移し空気遮断の密閉状態で貯留し、クラゲを嫌気性分
解により自然溶解し液状化するものであるために残留固
形廃棄物が大幅に減容化される。また、液状化物は消臭
薬剤と共に貯留タンクで配管によるポンプ循環するだけ
で脱臭処理が極めて安価に処理できるとともに、既存設
備である活性汚泥設備等で処理することでCOD濃度を
規定値以下の状態で放流処理することができる等の優れ
た効果を発揮する。
As is clear from the above results, according to the present invention, the jellyfish separated from the seawater intake line are transferred to a tank and stored in an air-tight closed state, and the jellyfish are naturally dissolved by anaerobic decomposition to form a liquid. The volume of residual solid waste is greatly reduced because it is made into a waste. In addition, liquefaction can be processed at a very low cost by simply circulating the liquefied chemicals together with the deodorant in the storage tank with a pump through a pipe, and the COD concentration can be kept below the specified value by processing with activated sludge equipment which is an existing equipment. It exhibits excellent effects such as being able to be discharged by the treatment.

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

【図1】海水取水ラインを示す概略断面図である。FIG. 1 is a schematic cross-sectional view showing a seawater intake line.

【図2】トラッシュピツト構造を示す概略斜視図であ
る。
FIG. 2 is a schematic perspective view showing a trash pit structure.

【図3】クラゲ処理状況を示す概略の全体フロー図であ
る。
FIG. 3 is a schematic overall flow chart showing a jellyfish processing situation.

【図4】実施例2における循環処理時間によるCOD濃
度変化を示す。
FIG. 4 shows a change in COD concentration according to a circulation treatment time in Example 2.

【符号の説明】[Explanation of symbols]

1 海水取水用ライン 3 取水ピットへの流入ライン 4 レーキバースクリーン 5 ロータリースクリーン 7 循環水ポンプ 8 スクリーン洗浄用ポンプ 13 水切りネットコンベヤー 14 固形塵芥物 17 密閉タンク 18 液状化物 20 残留固形物 21 貯留タンク 22 消臭薬剤 23 循環ポンプ 24 活性汚泥設備 25 構内排水ピット 1 Seawater intake line 3 Inflow line to the intake pit 4 rake bar screen 5 Rotary screen 7 circulating water pump 8 Screen cleaning pump 13 Draining net conveyor 14 Solid waste 17 closed tank 18 Liquid 20 Residual solid 21 Storage tank 22 Deodorant drug 23 Circulation pump 24 Activated sludge equipment 25 on-site drainage pit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 木島 佳克 兵庫県高砂市梅井6−4−1 電源開発株 式会社高砂火力発電所内 (72)発明者 橋川 忠和 兵庫県高砂市梅井6−4−1 電源開発株 式会社高砂火力発電所内 (72)発明者 坂元 隆志 沖縄県石川市赤崎三丁目4番1号 電源開 発株式会社石川火力発電所内 Fターム(参考) 4D004 AA02 CA17 CA48 CB04 CC11   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Yoshikatsu Kijima             6-4-1 Umei, Takasago, Hyogo Electric Power Development Co., Ltd.             Ceremony company Takasago Thermal Power Station (72) Inventor Tadakazu Hashikawa             6-4-1 Umei, Takasago, Hyogo Electric Power Development Co., Ltd.             Ceremony company Takasago Thermal Power Station (72) Inventor Takashi Sakamoto             3-4 Akasaki, Ishikawa-shi, Okinawa power supply opening             From Ishikawa Thermal Power Station Co., Ltd. F-term (reference) 4D004 AA02 CA17 CA48 CB04 CC11

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 海水を工業用冷却水として取水する際に
流入する混入クラゲ類の処理方法であって、海水取水ラ
インからクラゲや魚介類等の固形物を水切りネットコン
ベヤ等で水揚げ分離し、分離したクラゲ類をタンクに移
し空気遮断の密閉状態で数日間貯留しておき、クラゲが
嫌気性分解により自然溶解し液状化したことを確認して
から液状化物を分離し、該液状化物を消臭薬剤で脱臭処
理することを特徴とする海水取水ラインへの混入クラゲ
類の処理方法。
1. A method for treating mixed jellyfish that flows in when seawater is taken as industrial cooling water, wherein solids such as jellyfish and seafood are landed and separated from a seawater intake line using a draining net conveyor or the like. The separated jellyfish are transferred to a tank and stored for several days in an air-tight sealed state, and after confirming that the jellyfish spontaneously dissolved and liquefied by anaerobic decomposition, the liquefaction is separated and the liquefaction is removed. A method for treating jellyfish mixed in a seawater intake line, characterized by deodorizing with an odor chemical.
【請求項2】 消臭薬剤で脱臭処理した液状化物は、活
性汚泥設備等でCOD低減の無害化処理をすると共に、
タンクから液状化物を分離した後の減容化した残留固形
物は一般固形廃棄物として処理する請求項1記載の海水
取水ラインへの混入クラゲ類の処理方法。
2. The liquefied product deodorized with a deodorant chemical is subjected to a detoxifying process for reducing COD in an activated sludge facility or the like, and
The method for treating jellyfish mixed in a seawater intake line according to claim 1, wherein the volume-reduced residual solid matter after separating the liquefied material from the tank is treated as general solid waste.
【請求項3】 液状化物の脱臭処理は、タンク内で液状
化物に消臭薬剤を添加しポンプで循環処理するものであ
る請求項1又は2に記載の海水取水ラインへの混入クラ
ゲ類の処理方法。
3. The treatment of jellyfish mixed in the seawater intake line according to claim 1 or 2, wherein the deodorizing treatment of the liquefied material is to add a deodorant agent to the liquefied material in a tank and circulate the liquefied material with a pump. Method.
【請求項4】 消臭薬剤として、次亜塩素酸ソーダを使
用する請求項1〜3のいずれか1項に記載の海水取水ラ
インへの混入クラゲ類の処理方法。
4. The method for treating jellyfish mixed in a seawater intake line according to claim 1, wherein sodium hypochlorite is used as a deodorant.
JP2002030306A 2002-02-07 2002-02-07 Method for treating jellyfishes getting mixed into sea water intake line Pending JP2003225639A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002030306A JP2003225639A (en) 2002-02-07 2002-02-07 Method for treating jellyfishes getting mixed into sea water intake line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002030306A JP2003225639A (en) 2002-02-07 2002-02-07 Method for treating jellyfishes getting mixed into sea water intake line

Publications (1)

Publication Number Publication Date
JP2003225639A true JP2003225639A (en) 2003-08-12

Family

ID=27750355

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002030306A Pending JP2003225639A (en) 2002-02-07 2002-02-07 Method for treating jellyfishes getting mixed into sea water intake line

Country Status (1)

Country Link
JP (1) JP2003225639A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007000863A (en) * 2005-05-25 2007-01-11 Microbial Chem Res Found Apparatus and method of treating salt-containing waste liquid, and microorganism
JP2009240976A (en) * 2008-03-31 2009-10-22 Chugoku Electric Power Co Inc:The Jellyfish dissolver, jellyfish treatment system, and method for controlling jellyfish treatment system
CN111291582A (en) * 2020-03-04 2020-06-16 广西大学 RFID antenna optimal deployment method based on jellyfish group algorithm

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007000863A (en) * 2005-05-25 2007-01-11 Microbial Chem Res Found Apparatus and method of treating salt-containing waste liquid, and microorganism
JP2009240976A (en) * 2008-03-31 2009-10-22 Chugoku Electric Power Co Inc:The Jellyfish dissolver, jellyfish treatment system, and method for controlling jellyfish treatment system
CN111291582A (en) * 2020-03-04 2020-06-16 广西大学 RFID antenna optimal deployment method based on jellyfish group algorithm
CN111291582B (en) * 2020-03-04 2023-04-07 广西大学 RFID antenna optimal deployment method based on jellyfish group algorithm

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