JPS5864174A - Treatment of jellyfish - Google Patents

Treatment of jellyfish

Info

Publication number
JPS5864174A
JPS5864174A JP56164584A JP16458481A JPS5864174A JP S5864174 A JPS5864174 A JP S5864174A JP 56164584 A JP56164584 A JP 56164584A JP 16458481 A JP16458481 A JP 16458481A JP S5864174 A JPS5864174 A JP S5864174A
Authority
JP
Japan
Prior art keywords
jellyfish
catalyst
ion
copper
oxygen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP56164584A
Other languages
Japanese (ja)
Other versions
JPH0112555B2 (en
Inventor
Akira Tanaka
公 田中
Makoto Ikeda
誠 池田
Teruhiko Hirabayashi
平林 輝彦
Yoshiyuki Imakire
今給黎 義之
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.)
Nippon Steel Eco Tech Corp
Original Assignee
Nittetsu Kakoki KK
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 Nittetsu Kakoki KK filed Critical Nittetsu Kakoki KK
Priority to JP56164584A priority Critical patent/JPS5864174A/en
Publication of JPS5864174A publication Critical patent/JPS5864174A/en
Publication of JPH0112555B2 publication Critical patent/JPH0112555B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To change the organic substance of jellyfish into a soluble state and to substantially annihilate them in the end, by treating the jellyfish in the presence of free oxygen at a specified temperature range for a proper time under pressure enough to maintain a liquid phase. CONSTITUTION:Jellyfish are treated in the presence of free oxygen at a temperature of 150-300 deg.C under pressure enough to maintain a liquid phase by a catalyst or without a catalyst for a proper time (e.g. 0.2-2hr), to change the organic substance of the jellyfish into a soluble state and to substantially annihilate them in the end. An amount of oxygen necessary for the decomposition is preferably above at least a value equivalent to the TOD substance constituting the jellyfish to obtain a more complete decomposition rate. When a catalyst is used, the one which exists as a copper or copper complex ion in the reaction system is preferably used, and the necessary addition amount of the copper catalyst is prefferably about 100-1,000ppm as Cu<++> ion. The concentration, separation and cyclic reuse of dissolved cupric ion can be performed by slightly adjustment of the Cu<++> ion in the waste water and then treating it with weakly acidic cation exchange resin.

Description

【発明の詳細な説明】 くは海月を大量に処理して消滅させる方法に関する。[Detailed description of the invention] It is about how to process and eliminate Kaigetsu in large quantities.

海月は水母とも書き主として腔腸動物門、ハチクラゲ綱
の有性世代で自由遊泳型のものをさすが、外見の類似す
る2〜5の他の分類の動物も含めて総称されている0こ
れらのうちにはびぜんくらげ、えちぜんくらげ等の様に
食用となるものもあるが、時として大量に発生し魚網を
破ったり、電気くらげと俗称される刺胞の毒素が強烈で
海水温容に恐れられるカツオノエポシなどの如く有害な
ものもある。海月の害で近時特に注目されるのは、原子
力発電所あるいは火力発電所の取水口に集る海月のなす
害である。
Kaigetsu is also written as water mother, and mainly refers to the free-swimming sexual generation of the Coelenterata and the class Medusa, but it is also a general term that includes animals from 2 to 5 other classifications that have similar appearances. There are some jellyfish that are edible such as Bizen Jellyfish and Echizen Jellyfish, but they sometimes occur in large numbers and break fishing nets, and the toxins of the nematocysts, commonly known as electric jellyfish, are so strong that the temperature of the seawater increases. Some are harmful, such as the feared bonito snail. One of the harmful effects of sea moons that has recently attracted particular attention is the harm caused by sea moons that gather at the water intakes of nuclear power plants or thermal power plants.

上記の大容量ボイラーを使用する発電所は復水器等に大
量の冷却水を使用し、温水を排出する。
Power plants that use the large-capacity boilers mentioned above use large amounts of cooling water in condensers, etc., and then discharge hot water.

我国においてはこの冷却水取水の便宜上、殆どのボイラ
ー型発電所は海岸地域に設立され海水を冷却水として大
量に取水し、温排水として再び海中に戻している。然る
にとへに由々しい問題が発生するに至った。即ちこれら
発電所にとって枢要な取水口に時として大量の海月が蝟
集し取水を困難とするのみならず、吸込まれたものは熱
交換器の伝面を汚染して能力を低下させるなど殆ど機能
停止を余儀なくされる程の害をも惹起する。海月の異常
発生の原因は不明とされているが、夏期の電力ピーク時
に海月の異常発生を見ることが多いため、特に問題は大
きく、電力業界共通の問題として犬きくクローズアップ
されている。対策としては取水口の周囲に網を張るなど
して進入を防ぐのであるが多い日には数百トンもの大群
が後から後から押寄せるので、これを掻き上げて取除か
ない時は網も無用の長物化する。所がこの掻き上げた海
月の処置が問題である。海月は海水浴の際よく経験する
様に見掛によらず保水性がよく容易に脱水されず、熱的
に脱水するにしてもまた焼却するにしても海月はその体
重の95〜98チが水から成るといわれており取扱上、
経済上困難である。
In Japan, most boiler-type power plants are built in coastal areas for the convenience of cooling water intake, and they take in large quantities of seawater as cooling water and return it to the sea as heated wastewater. However, a serious problem arose. In other words, a large amount of water sometimes collects in the water intakes that are important for these power plants, making it difficult to take in water, and what is inhaled contaminates the transmission surface of the heat exchanger and reduces its capacity, making it almost impossible to function. It also causes such harm that it is forced to stop. Although the cause of the abnormal occurrence of Kaigetsu is said to be unknown, it is a particularly serious problem as abnormal occurrences of Kaigetsu are often seen during the summer power peak, and it is being closely focused on as a common problem in the electric power industry. . As a countermeasure, we put a net around the water intake to prevent them from entering, but on busy days, large swarms of hundreds of tons come rushing in from behind, so if we don't rake them up and remove them, we don't have to put the nets in. It becomes a useless thing. However, the problem lies in what to do with this raised seaweed. As is often experienced when swimming in the sea, Kaigetsu has a good water retention capacity and does not dehydrate easily despite its appearance, and whether it is thermally dehydrated or incinerated, Kaigetsu loses 95 to 98 inches of its body weight. is said to consist of water, so when handling it,
It is economically difficult.

海産物とはいえ大量の死体を近海沿岸部に投棄すること
は許されない。そこで従来とられた方法は掻き上げた海
月を一定の貯蔵場に集積し自然の浄化力に1つことであ
ったが、この場合時として腐敗し悪臭公害源となるのみ
ならず、数日間の大量蝟集があれば貯蔵も困難となり発
電停市の非常時態もまた避けられなかった。
Even though they are seafood, it is not permissible to dump large quantities of carcasses in coastal areas. The conventional method for this purpose was to accumulate the scraped up seaweed in a certain storage area to utilize its natural purifying power. If there was a large amount of waste collected, it would be difficult to store it, and a state of emergency in the city without power generation was inevitable.

本発明は以上の海月によってもたらされる困難を解決す
るユニークな方法を提供するものである。
The present invention provides a unique method to overcome the difficulties posed by the above problems.

従来海月は発生学的には興味をもって研究されて来たが
、その他の化学的成分についてはあまり知られておらず
。主にキチン質からなるとする説もある。キチン質とは
アミノ多糖類と蛋白質とからなる複合体であり、各種溶
剤に難溶性であるばかりで々〈化学的には相当程度不活
性であるとされている。これを低温で焼却する時は悪臭
を発生するが、水を焼却するに等しいエネルギーの損失
のみならず高温で焼却すればアミン基よりツユエルNO
x を発生し易い。本発明者らはこの様に処理困難と考
えられている海月の大量処分方法について種々検討の結
果、これを遊離酸素の存在下150〜600℃の温度で
液相が保たれるのに充分な圧力の下に適当時間処理する
ことによって海月の有機物は可溶化し、ついには殆ど消
滅することを見出し、本願発明に到達した。以下本発明
の実施方法について述べる。
Until now, Kaigetsu has been studied with interest from an embryological standpoint, but not much is known about its other chemical components. There is also a theory that it consists mainly of chitin. Chitin is a complex consisting of aminopolysaccharides and proteins, and is not only poorly soluble in various solvents, but is also said to be fairly inert chemically. When incinerated at low temperatures, it emits a foul odor, but not only does it result in a loss of energy equivalent to incinerating water, but if it is incinerated at high temperatures, amine groups generate more NO.
x is likely to occur. As a result of various studies on mass disposal methods for Kaigetsu, which are considered to be difficult to process, the present inventors found that the method is sufficient to maintain a liquid phase at a temperature of 150 to 600°C in the presence of free oxygen. It was discovered that by treating under a certain pressure for an appropriate period of time, the organic matter in the seaweed becomes solubilized and eventually almost disappears, leading to the present invention. A method of implementing the present invention will be described below.

海月は時として直径0.5〜1m程の大きさに達するも
のがあるが、通常害をなすものは5〜20tYn程のも
のが多い。いづれにせよこれらの海月はゲル状を呈しこ
のま\処理するときは不均一な反応を起しやすいし、取
扱上も問題があるのでこれを解膠状態にすることが好ま
しい。
Sea moons sometimes reach a diameter of 0.5 to 1 m, but the ones that are usually harmful are about 5 to 20 tYn. In any case, these seaweeds have a gel-like appearance, and if they are processed immediately, they tend to cause uneven reactions, and there are also problems in handling, so it is preferable to bring them into a peptized state.

特に連続的に処理する時は前以ってミキサ一様の装置で
処理して・おくことが好ましい。回分処理の時は高速攪
拌によって比較的容易に反応器内でも分断されるが、反
応速度の面からみてミキサー程度の高速撹拌羽根で前以
って処理しておくことは極めて有効である。この様に処
理することによって海月は若干の浮遊懸濁質を含有する
乳状液となるが、これは分別することなく全量処理可能
である。反応処理に先立ってこの乳状液を1!#縮して
おくことは反応器の小型化に対して(j−効である。海
月を消滅させるための反応は遊離状酸素の存在下で行う
が、この目的のためには空気、純酸素、あるいは酸素富
化空気等が好適に用いられる。この分解に必要な酸素量
は、より完全な分解度を得るために海月を構成するTO
D物質に対して少くとも当量以上が好ましい。それ以下
の時は酸素不足のため冒い分解度は得られないし、不完
全分解によるCODあるいはBOD物質の溶存量、気相
あるいは液相中の悪臭物質の存在量の増加は避けられな
い。
In particular, when processing continuously, it is preferable to perform the processing in advance using a mixer-like device. During batch processing, high-speed stirring causes separation within the reactor relatively easily, but from the viewpoint of reaction speed, it is extremely effective to perform processing in advance using a high-speed stirring blade such as a mixer. By processing in this way, Kaigetsu becomes an emulsion containing some suspended solids, but this can be processed in its entirety without being separated. Before the reaction treatment, add 1! of this emulsion! # Keeping it compressed has a (j-effect) on downsizing the reactor.The reaction to annihilate Kaigetsu is carried out in the presence of free oxygen, but for this purpose air, pure Oxygen or oxygen-enriched air is preferably used.The amount of oxygen required for this decomposition is determined by the TO
It is preferable that the amount is at least equivalent to the amount of substance D. When the temperature is lower than that, a high degree of decomposition cannot be obtained due to lack of oxygen, and an increase in the dissolved amount of COD or BOD substances and the amount of malodorous substances in the gas phase or liquid phase due to incomplete decomposition is unavoidable.

連常1.5〜2当量あれば回分式の反応には充分である
が多いの(は特に差支えない。触媒を用いる場合は、反
応中に銅イオン又は銅鉛イオ/となって存在するものが
好適に用いられる。金属銅を用いても海月は分解によっ
てアンモニアを発生しゃすいアミノ糖類、あるいは蛋白
質類をその構成成分として含有することによりその汀効
性が極めて大きくなる。その地鉄、マンガンニッケル、
モリブデン等の遷移金属も触媒として用いうるが銅には
有効性が及ばない。銅触媒の必要添加量はCuF +イ
オンとして約、100〜1000 pI)m好ましくは
200〜600ppmあれば充分である。kれ以上あっ
ても効果は特に増大せず、排水処理上の困難性が増大す
る。排水中の1伺イオンは魚毒性もあり、好ましくない
が、木紬発明の場合処理後の排水のpHは4〜6附近の
場合が多いので、殆ど声調整をしなくても、あるいは僅
かの調整後弱酸性の陽イオン交換樹脂での処理によって
溶存銅イオンの濃縮分離、循環再使用が可能であり特に
問題はない。
A continuous amount of 1.5 to 2 equivalents is sufficient for a batch reaction, but there is no particular problem.When using a catalyst, copper ions or copper lead ions exist during the reaction. is suitably used. Even if metallic copper is used, its detergent effectiveness will be extremely high if it contains amino sugars or proteins that generate ammonia upon decomposition as its constituent components. manganese nickel,
Transition metals such as molybdenum can also be used as catalysts, but are less effective than copper. It is sufficient that the necessary amount of the copper catalyst added is about 100 to 1000 pI) m, preferably 200 to 600 ppm as CuF + ions. Even if the amount is more than k, the effect will not be particularly increased and the difficulty in treating wastewater will increase. Ions in wastewater are toxic to fish and are undesirable, but in the case of the Mokutsumugi invention, the pH of the wastewater after treatment is often around 4 to 6, so it can be used with little or no adjustment. After adjustment, the dissolved copper ions can be concentrated and separated by treatment with a weakly acidic cation exchange resin, and can be recycled and reused without any particular problem.

また硫化物系の銅相金属、処理剤も用いることが出来る
。反応温度は通常150〜500°Cの範囲であるが、
反応は200°C附近から急激に高まる。i s o 
’c以下では反応は不充分であり、3o o ’c以上
にしても特にメリットは少い。丑た帯留時間は通常0.
2〜2時間、好ましくは1〜1.5時間で充分である。
Sulfide-based copper phase metals and processing agents can also be used. The reaction temperature is usually in the range of 150 to 500°C,
The reaction increases rapidly from around 200°C. iso
If it is less than 'c, the reaction will be insufficient, and if it is more than 3o'c, there will be little benefit. Ushita retention time is usually 0.
2 to 2 hours, preferably 1 to 1.5 hours is sufficient.

勿論長ければ分解はより完全となる。この際の反応圧は
水蒸気圧以外に酸素分圧が必要であるが、空気を用いれ
ば高く、純酸紫を用いればより低くなる。回分式の場合
通常酸素分圧で初圧を10〜20気圧程度とすれば先づ
充分であるが、この酸素分圧の必要度は反応方式、条件
等によっても変化し、回分式でもガスのみ流通式とすれ
ば反応圧を下げることが可能となる。尚、触媒を特に用
いなくとも反応は進行し、触媒金属の後処理が不要であ
る点有利となるが一般に反応速度は稍々遅く、反応液中
に低級脂肪酸が残り易い。この様な自機酸は活性汚泥法
によって処理が可能であるが、電源立地は必ずしも敷地
面積に余裕がないので触媒を使用して一挙に処理をする
方がよい場合も多い。また触媒を使用しない場合、2次
的処理として電気化学的処理、過酸化水素、オゾン等に
よる総合処理も電源立地の地の利を生かして容易に行い
うる。
Of course, the longer it is, the more complete the decomposition will be. The reaction pressure at this time requires oxygen partial pressure in addition to water vapor pressure, but it will be higher if air is used, and lower if pure acid purple is used. In the case of a batch method, it is usually sufficient to set the initial oxygen partial pressure to about 10 to 20 atm, but the degree of necessity for this oxygen partial pressure varies depending on the reaction method, conditions, etc., and even in a batch method, only gas If a flow type is used, it becomes possible to lower the reaction pressure. The reaction proceeds even without the use of a catalyst, which is advantageous in that post-treatment of the catalytic metal is not required; however, the reaction rate is generally rather slow and lower fatty acids tend to remain in the reaction solution. Such organic acid can be treated by the activated sludge method, but since there is not necessarily enough site area for power source locations, it is often better to treat it all at once using a catalyst. In addition, when a catalyst is not used, electrochemical treatment, comprehensive treatment using hydrogen peroxide, ozone, etc. can be easily carried out as a secondary treatment by taking advantage of the location of the power source.

以上の様な分解条件の組合せによって海月の有機成分の
95%以上を1回の処理によって分解することは容易に
実施可能であり、産業上極めて有用な発明といえる。
By combining the above-mentioned decomposition conditions, it is possible to easily decompose more than 95% of the organic components of Kaigetsu in one treatment, and this invention can be said to be extremely useful industrially.

実施例 内容積1.5形の竪型攪拌式オートク、レーヴに、海月
をミキサーで5分間処理したものを秤量して入れ、空気
あるいは酸素で加圧の下、所定の温度及び時間触媒の存
在下あるいは非存在下に分解反応を行った。その結果を
第1表に示す。
Example: In a 1.5-inch internal volume vertical stirring autoclave, Reve, was weighed and put the Kaigetsu treated with a mixer for 5 minutes, and the catalyst was heated under pressure with air or oxygen at a predetermined temperature and time. The decomposition reaction was carried out in the presence or absence. The results are shown in Table 1.

第1表実験結果 *d    *(1*e    *d    $d試料
海月(め     150 250  35 400 
250添加水(め     250’150 365 
  0 150固形分濃度(2/β)     9.4
  156s、s   25  15.6触媒添加量*
a    400  400 400   0  20
0*b*b  *b  *C*C EΔガx?1kE(r’#aG)    49    
 so     4a     10    30反反
応度(’0)     280 225 280 28
0 180反応時間(mim)      90  9
0  90  90  150分解液π)C(m死) 
    2   74  325  36  300分
解液pH4,34,76,6−− 注* a  mg(u2+屑 *b 空気 *C酸素 *d みずくらげ(乾燥固型分25%)*e 市販食用
ひぜんくらげを水で脱塩したもの(固型分10%) 特許出願人 日鉄化工機株式会社
Table 1 Experimental results *d *(1*e *d $dSample 150 250 35 400
250 added water (me 250'150 365
0 150 Solid content concentration (2/β) 9.4
156s, s 25 15.6 Catalyst addition amount*
a 400 400 400 0 20
0*b*b *b *C*C EΔgax? 1kE(r'#aG) 49
so 4a 10 30 reaction degree ('0) 280 225 280 28
0 180 reaction time (mim) 90 9
0 90 90 150 decomposition liquid π)C (m death)
2 74 325 36 300 decomposed solution pH 4,34,76,6-- Note*a mg(u2+waste*b air *Coxygen*d water jellyfish (dry solid content 25%)*e commercially available edible water jellyfish (solid content 10%) Patent applicant Nippon Steel Kakoki Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] (1)海月を遊離酸素の存在下150〜500℃の温度
で液相が保たれるのに充分な圧力の下に無触媒あるいは
有触媒で処理することを特徴とする海月の処理方法。
(1) A method for treating seaweed, which is characterized by treating seaweed in the presence of free oxygen, at a temperature of 150 to 500°C, under sufficient pressure to maintain a liquid phase, either without or with a catalyst. .
(2)海月の処理が銅触媒の存在下に行われる特許請求
の範囲第(1)項に従う方法
(2) The method according to claim (1), in which the treatment of seaweed is carried out in the presence of a copper catalyst.
(3)海月がスラリー化されて処理されることを特徴と
する特許請求の範囲第(1)項あるいは第(2)項に従
う方法。
(3) A method according to claim (1) or (2), characterized in that the sea moon is processed as a slurry.
JP56164584A 1981-10-15 1981-10-15 Treatment of jellyfish Granted JPS5864174A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56164584A JPS5864174A (en) 1981-10-15 1981-10-15 Treatment of jellyfish

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56164584A JPS5864174A (en) 1981-10-15 1981-10-15 Treatment of jellyfish

Publications (2)

Publication Number Publication Date
JPS5864174A true JPS5864174A (en) 1983-04-16
JPH0112555B2 JPH0112555B2 (en) 1989-03-01

Family

ID=15795943

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56164584A Granted JPS5864174A (en) 1981-10-15 1981-10-15 Treatment of jellyfish

Country Status (1)

Country Link
JP (1) JPS5864174A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63111992A (en) * 1986-10-28 1988-05-17 Ngk Insulators Ltd Treatment of jellyfish gathering to intake
JP2002153837A (en) * 2000-11-17 2002-05-28 Ishikawajima Harima Heavy Ind Co Ltd Treatment method and treatment equipment for jellyfish
JP2009534172A (en) * 2006-04-19 2009-09-24 オテヴェ・ソシエテ・アノニム Method and corresponding equipment for oxidizing wastewater heated essentially by pyrophoricity by a wet process

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63111992A (en) * 1986-10-28 1988-05-17 Ngk Insulators Ltd Treatment of jellyfish gathering to intake
JPH0144112B2 (en) * 1986-10-28 1989-09-26 Ngk Insulators Ltd
JP2002153837A (en) * 2000-11-17 2002-05-28 Ishikawajima Harima Heavy Ind Co Ltd Treatment method and treatment equipment for jellyfish
JP2009534172A (en) * 2006-04-19 2009-09-24 オテヴェ・ソシエテ・アノニム Method and corresponding equipment for oxidizing wastewater heated essentially by pyrophoricity by a wet process

Also Published As

Publication number Publication date
JPH0112555B2 (en) 1989-03-01

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