JPH0824511B2 - Method and apparatus for treating aquaculture water - Google Patents

Method and apparatus for treating aquaculture water

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Publication number
JPH0824511B2
JPH0824511B2 JP18181991A JP18181991A JPH0824511B2 JP H0824511 B2 JPH0824511 B2 JP H0824511B2 JP 18181991 A JP18181991 A JP 18181991A JP 18181991 A JP18181991 A JP 18181991A JP H0824511 B2 JPH0824511 B2 JP H0824511B2
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JP
Japan
Prior art keywords
water
heat
aquaculture
air
cooling
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
JP18181991A
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Japanese (ja)
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JPH053736A (en
Inventor
欽吾 宮原
Original Assignee
株式会社スワーク
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Priority to JP18181991A priority Critical patent/JPH0824511B2/en
Publication of JPH053736A publication Critical patent/JPH053736A/en
Publication of JPH0824511B2 publication Critical patent/JPH0824511B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Farming Of Fish And Shellfish (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、海洋性或いは淡水性の
魚介類又は海草類等からなる多品種の水産生物を各種疾
病にかかることなく適確に養殖することができる水産養
殖水の処理方法およびその装置に関する。
FIELD OF THE INVENTION The present invention relates to a method for treating aquaculture water capable of appropriately cultivating a variety of aquatic products of marine or freshwater seafood, seaweed, etc. without suffering from various diseases. And its equipment.

【0002】[0002]

【従来の技術】従来、海洋性或いは淡水性の魚介類又は
海草類等からなる多品種の水産生物を海洋或いは淡水中
に周囲を囲んで形成した養殖用溜め或いは飼育池内に収
容して、前記水産生物を養殖水中において養殖する方法
は、本出願前、一般に広く用いられて周知である。
2. Description of the Related Art Conventionally, a variety of aquatic products of marine or freshwater seafood, seaweeds, etc. have been housed in an aquaculture reservoir or a pond formed around the sea or freshwater, and the aquatic product has been stored. The method of culturing organisms in culture water is widely used and well known before the filing of the present application.

【0003】[0003]

【発明が解決しようとする課題】ところで、従前のこの
種水産生物の養殖方法においては、養殖水の殺菌処理を
何等施さないので、養殖中の水産生物は水質の汚染等に
より病原菌が繁殖され、各種疾病が多発し、これが原因
で死滅する事故が生じた。そこで、これが解決を図るた
めに、養殖水に各種薬剤を投与して病原菌が発生するの
を予防していた。しかしながら、前記の如く養殖水への
薬剤等の投与を何回となく反復すると、溶解した薬剤が
水産生物の体内に蓄積されて汚染され、食用に供するこ
とができなくなるという弊害を招くことになる。一方、
水産生物の養殖の生産性を向上させるために、養殖水を
ボイラにより得られた温水の間接的な熱交換作用で加温
させたり或いは紫外線殺菌灯を用いて養殖水の殺菌を行
う方法が試みられているが、かかる方法では施設費や維
持費が高くつき、一般に使用することができない。した
がって、今後の水産生物の養殖に際しては、安価なコス
トで、しかも薬剤投与やボイラ等の間接熱交換作用を使
用することなく無菌化された大量の養殖水を簡単な方法
により得ることを提供することが水産生物の養殖上重要
な要件の一つであるは勿論のこと、養殖水の水温を常に
水産生物の養殖に適した温度に管理することや養殖水自
体が水産生物の生息に十分な酸素を含んだものであるこ
とも重要な問題である。
By the way, in the conventional method for cultivating this kind of aquatic product, since no sterilization treatment of the aquatic water is performed, the aquatic product during cultivation is propagated with pathogenic bacteria due to contamination of water quality, Various illnesses occurred frequently, resulting in death. Therefore, in order to solve this problem, various chemicals were administered to the culture water to prevent the occurrence of pathogenic bacteria. However, if the administration of the drug or the like to the aquaculture water is repeated many times as described above, the dissolved drug will be accumulated in the body of the aquatic product and contaminated, resulting in the adverse effect that it cannot be used for food. . on the other hand,
In order to improve the productivity of aquaculture of aquatic products, a method of heating the aquaculture water by indirect heat exchange of hot water obtained by a boiler or sterilizing the aquaculture water using an ultraviolet sterilization lamp is tried. However, such a method requires high facility costs and maintenance costs and cannot be generally used. Therefore, when aquaculture of future aquatic products is provided, it is possible to obtain a large amount of sterilized aquaculture water by a simple method at a low cost and without using indirect heat exchange action such as drug administration or boiler. This is not only one of the important requirements for aquaculture of aquatic products, but it is necessary to always control the temperature of the aquaculture water to a temperature suitable for aquaculture of aquatic products and the aquaculture water itself is sufficient for the aquatic products to inhabit. The fact that it contains oxygen is also an important issue.

【0004】本発明は、流下する原水を焔上する燃焼ガ
スと直接接触せしめる簡単な加熱殺菌処理手段により、
薬剤等の投与或いは間接加熱手段等を一切使用すること
なく無菌化された大量の養殖水を瞬時に量産するための
水産養殖水の処理方法およびその装置を得ることを目的
としており、さらに、加熱殺菌処理された加熱水は保熱
滅菌槽において、より一層の滅菌化を図ると共に加熱水
はさらに流通する空気と直接接触せしめて冷却と曝気作
用を同時に行って養殖に適した水温と生息に十分な酸素
量を補給できる水産養殖水の処理方法およびその装置を
提供することを目的としている。
According to the present invention, a simple heat sterilization treatment means for directly bringing the raw water flowing down into direct contact with the combustion gas rising in the flame,
The purpose is to obtain a method for treating aquaculture water and a device therefor for instantly mass-producing a large amount of sterilized aquaculture water without using any drug or indirect heating means. The sterilized heated water is further sterilized in the heat retention sterilization tank, and the heated water is brought into direct contact with the circulating air to perform cooling and aeration at the same time. It is an object of the present invention to provide a method for treating aquaculture water and an apparatus therefor capable of supplementing a large amount of oxygen.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に、本発明の水産養殖水の処理方法においては、流下す
る原水に、焔上する燃焼ガスを直接接触させて加熱し、
加熱殺菌された養殖水としたものである。
In order to achieve the above object, in the method for treating aquaculture water of the present invention, the raw water flowing down is directly contacted with the combustion gas to be flamed, and heated.
It is the culture water that has been sterilized by heating.

【0006】そして、加熱して得られた加熱水は一旦保
熱滅菌槽に収容してさらに滅菌処理したものである。そ
の上、加熱して得られた加熱水は流通する空気と直接接
触するよう流下せしめて空冷曝気したものである。
The heated water obtained by heating is once stored in a heat-retaining sterilization tank and further sterilized. In addition, the heated water obtained by heating is flown down so as to come into direct contact with the circulating air and aerated with air cooling.

【0007】また、本発明の水産養殖水の処理装置にお
いては、本体内の上段に散水器および熱交換層を設けた
熱交換室を、下段にバーナの燃焼口を臨ませた燃焼室を
立体的に配設した水加熱処理装置と、周囲を保温加工し
た保熱滅菌槽とを通水管を介し接続したものである。
Further, in the aquaculture water treatment apparatus of the present invention, the heat exchange chamber provided with the sprinkler and the heat exchange layer in the upper stage of the main body and the combustion chamber facing the combustion port of the burner in the lower stage are three-dimensional. The water heat treatment device that is arranged in a special manner and a heat retaining sterilization tank whose periphery is heat treated are connected through a water pipe.

【0008】さらに、本体内の上段に散水器および熱交
換層を設けた熱交換室を、下段にバーナの燃焼口を臨ま
せた燃焼室を立体的に配設した水加熱処理装置と、本体
内の上段に散水器および熱交換層を設けた冷却室を、下
段に送風機の送風口を臨ませた曝気室を設けた空冷曝気
装置とを通水管を介し接続したものである。
Further, a water heat treatment apparatus in which a heat exchange chamber having a water sprinkler and a heat exchange layer in the upper stage of the main body and a combustion chamber facing the combustion port of the burner in the lower stage are three-dimensionally arranged, and the main body A cooling chamber having a sprinkler and a heat exchange layer in the upper part of the inside is connected via a water pipe to an air-cooling aerating device having an aeration chamber facing the blower port of a blower in the lower part.

【0009】また、水加熱処理装置と空冷曝気装置との
間に保熱滅菌槽を配設したものである。
Further, a heat-retaining sterilization tank is provided between the water heat treatment device and the air-cooling aeration device.

【0010】その上、水加熱処理装置と空冷曝気装置と
の間に配設した保熱滅菌槽の給水側は水加熱処理装置の
燃焼室に、また排水側は空冷曝気装置の散水器にそれぞ
れ接続したものである。
In addition, the water supply side of the heat retention sterilization tank disposed between the water heating treatment device and the air cooling aeration device is the combustion chamber of the water heating treatment device, and the drain side is the sprinkler of the air cooling aeration device. It is connected.

【0011】[0011]

【作用】図1において、原水(水道水、井戸水、遊水池
の水、海水等)を散水器5により熱交換室4内に設けた
熱交換層3上へ均等量宛散水すると同時にバーナ9を運
転して、その燃焼ガスを燃焼口10より燃焼室8内へ噴
出させる。さすれば、原水は熱交換層3内を紆余曲折し
ながら均等に流下した後、燃焼室8中を通って下部へ落
入されると共に燃焼ガスは原水の流下方向と逆に燃焼室
8より熱交換層3中を均等状態のもとに焔上し、最後に
水加熱処理装置1の排出口15より外部に排出される。
したがって、上方より下方に向け流下する原水と、下方
より上方に向け焔上する燃焼ガスとは、その流下および
焔上過程において何回となく直接接触され、瞬間的に加
熱水となり、殺菌処理されて無菌状態の加熱殺菌水とな
りながら出水口11より出て、通水管12および三方弁
13を経て適宜の場所に供給処理され、水産生物の養殖
水として使用される。
In FIG. 1, raw water (tap water, well water, reservoir water, seawater, etc.) is sprayed by the sprinkler 5 onto the heat exchange layer 3 provided in the heat exchange chamber 4 at the same time as the burner 9 is sprayed. The fuel cell is operated to eject the combustion gas from the combustion port 10 into the combustion chamber 8. Then, after the raw water uniformly flows down through the heat exchange layer 3 while twisting and bending, the raw water passes through the combustion chamber 8 and drops downward, and the combustion gas flows from the combustion chamber 8 in the reverse direction of the raw water. The heat exchange layer 3 is flamed in an even state, and finally discharged from the discharge port 15 of the water heat treatment apparatus 1 to the outside.
Therefore, the raw water flowing downwards from above and the combustion gas burning upwards from below are in direct contact with each other several times in the process of flowing down and flames, and become instantaneous heated water for sterilization treatment. The heat-sterilized water in the aseptic state is discharged from the water outlet 11 and supplied to an appropriate place through the water pipe 12 and the three-way valve 13 to be used as aquaculture water for aquatic products.

【0012】図2においては、図1の水加熱処理装置1
により加熱殺菌処理された加熱水は通水管12および三
方弁13を経て周囲を保温材17により保温された保熱
滅菌槽16内へ供給されると同時に一定時間保熱状態に
貯留される。したがって、水加熱処理装置1より保熱滅
菌槽16内に供給された加熱水の水温が比較的低温(例
えば50℃前後)の場合にあっても、一定時間に亘る保
熱作用でより一層の滅菌効果が達成される。すなわち、
ミズカビ病の病原菌である水生菌は水温20℃以上にな
るとその成長が停止して、ミズカビ病等の発生が激減す
ることが知られているので、本発明方法により得られた
加熱水の水温が50℃程度の場合にあっても、保熱滅菌
槽16内における保熱状態を維持すれば、殆どの病原菌
の生存は困難となる。したがって、保熱滅菌槽16にお
いて滅菌処理された加熱処理水は排水管19より水産生
物(例えば海洋性或いは淡水性の魚介類又は海草類等)
を養殖するための養殖水として供給される。
In FIG. 2, the water heat treatment apparatus 1 of FIG.
The heated water sterilized by heat is supplied to the heat-retaining sterilization tank 16 whose surroundings are kept warm by the heat-retaining material 17 through the water pipe 12 and the three-way valve 13, and at the same time stored in a heat-retaining state for a certain period of time. Therefore, even when the temperature of the heating water supplied from the water heat treatment apparatus 1 into the heat retention sterilization tank 16 is relatively low (for example, around 50 ° C.), the heat retention action for a certain period of time further improves the heat treatment. A sterilization effect is achieved. That is,
It is known that the aquatic bacterium, which is the pathogen of the mildew disease, stops its growth at a water temperature of 20 ° C. or higher and the occurrence of the mildew disease is drastically reduced. Therefore, the water temperature of the heated water obtained by the method of the present invention is Even if the temperature is about 50 ° C., maintaining the heat-retaining state in the heat-retaining sterilization tank 16 makes it difficult for most pathogenic bacteria to survive. Therefore, the heat-treated water that has been sterilized in the heat retention sterilization tank 16 is a water product (for example, marine or freshwater seafood or seagrass) from the drain pipe 19.
Is supplied as aquaculture water for aquaculture.

【0013】図3においては、図1の水加熱処理装置1
により加熱殺菌処理された加熱水は通水管12、三方弁
13、ポンプ31を経て空冷曝気装置20の散水器24
に供給され、熱交換層22上へ均等量宛散水される。と
ころで、上記の如き散水状態時にあっては、送風機26
の運転で起風された空気は曝気室25内に勢いよく噴送
され、次いで、前記空気は熱交換層22、冷却室23を
通って装置20外に排気されるように流通しているの
で、流下する加熱水と上方に向け流通する空気とは、冷
却室23、熱交換層22および曝気室25の通過過程に
おいて何回となく直接接触されて速やかに冷却されると
同時に曝気され、多量の酸素を含んだ低温の養殖水とな
りながら適宜養殖場所まで給水される。したがって、図
3に示された水産養殖水の処理装置によれば、空気送風
量の単なる調整操作により加熱水の水温を水産生物の養
殖適正水温(例えば15℃〜20℃)とすることができ
ると同時に水加熱処理装置1で得られた加熱水が燃焼ガ
スとの直接接触加熱作用で溶存酸素量が例えば4.5〜
6.5mg/L程度に減少しても、空冷曝気装置20に
よる空冷曝気作用で原水の溶存酸素量、例えば7.5〜
9.5mg/L程度まで増加できるよう自動的に酸素を
補給し、もって、養殖水として使用した場合に水産生物
の生息を助長して有効的な養殖作業を達成できる。
In FIG. 3, the water heat treatment apparatus 1 of FIG.
The heated water that has been sterilized by heating passes through the water pipe 12, the three-way valve 13, and the pump 31, and the sprinkler 24 of the air-cooling aeration device 20.
And is sprayed onto the heat exchange layer 22 in an equal amount. By the way, in the sprinkling state as described above, the blower 26
The air blown by the operation of is vigorously jetted into the aeration chamber 25, and then the air flows through the heat exchange layer 22 and the cooling chamber 23 so as to be discharged to the outside of the device 20. The flowing heated water and the air flowing upward are contacted with each other several times in the process of passing through the cooling chamber 23, the heat exchange layer 22 and the aeration chamber 25 to be rapidly cooled and aerated at the same time. The low temperature aquaculture water containing oxygen is supplied to the aquaculture site as appropriate. Therefore, according to the aquaculture water treatment apparatus shown in FIG. 3, the water temperature of the heated water can be set to the appropriate water temperature for aquaculture of the aquatic product (for example, 15 ° C. to 20 ° C.) by simply adjusting the air blowing amount. At the same time, the heated water obtained in the water heat treatment apparatus 1 has a dissolved oxygen content of, for example, 4.5 to 5 due to the direct contact heating action with the combustion gas.
Even if it is reduced to about 6.5 mg / L, the amount of dissolved oxygen in the raw water, for example, 7.5 due to the air-cooling aeration action of the air-cooling aeration device 20.
Oxygen is automatically replenished so that the amount can be increased up to about 9.5 mg / L. Therefore, when used as aquaculture water, the aquaculture work can be achieved by promoting the inhabitation of aquatic products.

【0014】図4においては、図1の水加熱処理装置1
により加熱殺菌処理された加熱水は保熱滅菌槽16に供
給され、該保熱滅菌槽16内において一定時間保温状態
に維持される間にさらに滅菌処理される。そして、滅菌
処理された加熱処理水は空冷曝気装置20に供給され、
該空冷曝気装置20により適正水温および適正な溶存酸
素量を有する養殖水に処理される。したがって、図4に
処理された水産養殖水の処理装置によれば、水加熱処理
装置1により得られた加熱水の水温が比較的低温であっ
ても保熱滅菌槽16において十分に滅菌処理して無菌加
熱水となし、適正水温のしかも適性量の酸素を溶存せし
めた最適の養殖水を得ることができる。
In FIG. 4, the water heat treatment apparatus 1 of FIG.
The heated water sterilized by heating is supplied to the heat-retaining sterilization tank 16 and further sterilized while being kept in a heat-retaining state for a certain time in the heat-retaining sterilization tank 16. Then, the sterilized heat-treated water is supplied to the air-cooling aerator 20,
The air-cooled aeration device 20 treats aquaculture water having a proper water temperature and a proper dissolved oxygen amount. Therefore, according to the treatment apparatus for aquaculture water treated in FIG. 4, even if the temperature of the heated water obtained by the water heating treatment apparatus 1 is relatively low, the heat-retaining sterilization tank 16 is sufficiently sterilized. As a result, it is possible to obtain the optimum aquaculture water that has a proper water temperature and has an appropriate amount of oxygen dissolved therein.

【0015】[0015]

【実施例】図1に示されたものは、流下する原水(水道
水、井戸水、遊水池の水、海水等)に、燃焼ガスを直接
接触させて加熱殺菌したことで、水産生物、例えば海洋
性或いは淡水性の魚介類又は海草類等の多品種の水産生
物を養殖するために用いられる無菌状態の養殖水を連続
して量産することができる水産養殖水の処理装置の第1
実施例であって、該第1実施例の水産養殖水の処理装置
は、以下に記載された水加熱処理装置1により構成され
ている。すなわち、内部を空胴とした断面任意形状の本
体2内の上段位置にセラミック材料或いは金属材料等か
らなる耐熱性の熱交換層3を配設して本体2の上段に熱
交換室4を区画形成すると共に、熱交換室4内の上位に
は散水器5が配設されている。そして、前記散水器5に
はポンプ7を途中に設けた給水管6の先端側が接続され
ている。本体2の下段は空胴の燃焼室8に形成され、議
燃焼室8の一側にはバーナ9を取外し自在となるように
配設してバーナ9の燃焼口10を燃焼室8内に臨ませて
ある。本体2の下部に開口された出水口11には、三方
弁13を途中に設けた通水管12を接続せしめて、三方
弁13の自動切替作動で出水口11より排出された高温
の加熱殺菌状態の養殖水を養殖場所へ供給せしめたり、
或いは養殖水の水温が所定温度(例えば50℃)以下の
場合には排水管14を経て外部に排水せしめる。そし
て、本体2の頂部には低温となった燃焼ガスの排気ガス
の排出口15が開口されている。
[Examples] In the example shown in FIG. 1, raw water (tap water, well water, water in a retaining basin, seawater, etc.) that flows down is directly contacted with a combustion gas for heat sterilization to obtain a water product, for example, ocean. A first aquaculture water treatment device capable of continuously mass-producing sterile aquaculture water used for aquaculture of various types of aquatic products such as natural or freshwater seafood or seaweed
The aquaculture water treatment apparatus according to the first embodiment is constituted by a water heating treatment apparatus 1 described below. That is, a heat-resistant heat exchange layer 3 made of a ceramic material, a metal material, or the like is disposed in an upper position of a main body 2 having an arbitrary cross-section with a hollow inside, and a heat exchange chamber 4 is defined in the upper stage of the main body 2. While being formed, a water sprinkler 5 is disposed above the heat exchange chamber 4. The water sprinkler 5 is connected to the tip end side of a water supply pipe 6 provided with a pump 7 on the way. The lower stage of the main body 2 is formed in a hollow combustion chamber 8. The burner 9 is disposed on one side of the main combustion chamber 8 so that the burner 9 can be detached, and the combustion port 10 of the burner 9 is placed inside the combustion chamber 8. I have it. The water outlet 11 opened at the bottom of the main body 2 is connected to a water pipe 12 provided with a three-way valve 13 in the middle, and a high-temperature heat sterilization state is discharged from the water outlet 11 by the automatic switching operation of the three-way valve 13. Supply the aquaculture water of
Alternatively, when the water temperature of the aquaculture water is lower than a predetermined temperature (for example, 50 ° C.), it is drained to the outside through the drain pipe 14. An exhaust port 15 for exhaust gas of the combustion gas, which has become low in temperature, is opened at the top of the main body 2.

【0016】図2に示されたものは、図1に示された水
加熱処理装置1により得られた加熱水を保熱滅菌槽16
へ収容して、さらに滅菌された養殖水を連続して量産す
ることができる第2実施例の水産養殖水の処理装置であ
って、第2実施例のものは、図1に示された第1実施例
の水加熱処理装置1と保熱滅菌槽16とにより構成され
ている。したがって、水加熱処理装置1は、その構成が
第1実施例の構成と全く同一であるからその説明を省略
し、保熱滅菌槽16と水加熱処理装置1との接続構成に
ついて説明する。保熱滅菌槽16は、周囲を適宜の保温
材17で囲み、内部に収容した加熱水を保熱状態のもと
に維持させて、より一層の滅菌効果を高めるようにした
ものであり、前記保熱滅菌槽16は保温材17からなる
蓋18の被蓋で略密封状態となる。したがって、保熱滅
菌槽16内に収容した加熱水の水温が50℃程度の保熱
状態を維持することができれば、ミズカビ病の病原菌で
ある水生菌等は、水温20℃以上になるとその成長が停
止するため、滅菌状態の養殖水を簡単に量産することが
できる。水加熱処理装置1の出水口11に一端が接続さ
れ、その途中に三方弁13を備えた通水管12の他端は
蓋18を貫通して保熱滅菌槽16内に挿入開口せしめる
と共に、保熱滅菌槽16の下部一側には滅菌された養殖
水の排水管19が接続されている。
As shown in FIG. 2, the heated water obtained by the water heat treatment apparatus 1 shown in FIG.
The apparatus for treating aquaculture water according to the second embodiment, which is capable of continuously mass-producing and further sterilizing the culture water after being stored in It is composed of a water heat treatment apparatus 1 and a heat retention sterilization tank 16 of one embodiment. Therefore, the structure of the water heat treatment apparatus 1 is completely the same as that of the first embodiment, and therefore the description thereof will be omitted, and the connection structure between the heat retention sterilization tank 16 and the water heat treatment apparatus 1 will be described. The heat-retaining sterilization tank 16 is such that the periphery thereof is surrounded by an appropriate heat-retaining material 17, and the heated water contained therein is maintained under a heat-retaining state to further enhance the sterilization effect. The heat-retaining sterilization tank 16 is substantially sealed by a lid 18 made of a heat-insulating material. Therefore, if the water temperature of the heated water stored in the heat-retaining sterilization tank 16 can be maintained at a heat-retaining state of about 50 ° C., the growth of aquatic bacteria, which are the pathogens of the fungus mold, at 20 ° C. or above Since it is stopped, sterile aquaculture water can be easily mass-produced. One end is connected to the water outlet 11 of the water heat treatment apparatus 1, and the other end of the water passage 12 provided with a three-way valve 13 in the middle of the water heat treatment apparatus 1 penetrates the lid 18 and is inserted into the heat sterilization tank 16 for opening. A drain pipe 19 of sterilized aquaculture water is connected to one side of the lower portion of the heat sterilization tank 16.

【0017】図3に示されたものは、図1に示された水
加熱処理装置1により得られた加熱水を空気曝気装置2
0に供給して適正養殖水温に冷却すると同時に、水加熱
処理装置1において減少した溶存酸素量を水産生物の生
息に十分な酸素を含んだ養殖水を量産することができる
第3実施例の水産養殖水の処理装置であって、第3実施
例のものは、図1に示された第1実施例の水加熱処理装
置1と空冷曝気装置20とにより構成されている。した
がって、水加熱処理装置1はその構成が第1実施例の構
成と全く同一であるから、その構成の説明を省略し、空
冷曝気装置20と水加熱処理装置1との接続構成につい
て説明する。前記空冷曝気装置20は、内部を空胴とし
た断面任意形状の本体21内の上段位置にセラミック材
料或いは金属製材料等からなる熱交換層22を配設して
本体21の上段に冷却室23を区画形成すると共に、冷
却室23内の上位には、水加熱処理装置1の通水管12
の先端側をポンプ31を介し接続した散水器24が配設
されている。本体21の下段は空胴の曝気室25に形成
され、該曝気室25の一側には送風機26を取外し自在
に装着せしめて送風機26の送風口27を曝気室25内
に臨ませてある。そして、本体21の下部に開口した出
水口28には、処理水を適宜の場所に供給するための給
水管29が接続され、また本体21の頂部には排気口3
0を開口して構成されている。したがって、第3実施例
に示された水産養殖水の処理装置によれば、水加熱処理
装置1により得られた加熱水がたとえ高温の殺菌水であ
っても、冷却室23内における熱交換作用により養殖適
正水温(例えば、15℃〜20℃)となるよう水温調節
ができる許りか、水加熱処理装置1において減少した溶
存酸素量、例えば4.5〜6.5mg/L程度を曝気作
用で原水の溶存酸素量、例えば7.5〜9.5mg/L
程度の水準まで補給して水産生物の養殖水として最適の
ものとすることができる。
In the apparatus shown in FIG. 3, the heated water obtained by the water heat treatment apparatus 1 shown in FIG.
No. 0 and cooled to an appropriate aquaculture water temperature, and at the same time, aquaculture water containing a sufficient amount of dissolved oxygen reduced in the water heat treatment apparatus 1 to produce aquaculture water having sufficient oxygen for inhabiting aquatic products can be mass produced. The aquaculture water treatment apparatus of the third embodiment comprises the water heating treatment apparatus 1 and the air-cooling aeration apparatus 20 of the first embodiment shown in FIG. Therefore, the structure of the water heat treatment apparatus 1 is exactly the same as that of the first embodiment, and therefore the description of the structure is omitted, and the connection configuration of the air-cooling aeration apparatus 20 and the water heat treatment apparatus 1 will be described. In the air-cooling aeration device 20, a heat exchange layer 22 made of a ceramic material or a metal material is disposed at an upper stage position in a main body 21 having an internal cavity and having an arbitrary cross section, and a cooling chamber 23 is provided in the upper stage of the main body 21. And the upper portion of the cooling chamber 23, the water pipe 12 of the water heat treatment apparatus 1 is formed.
A water sprinkler 24 having the tip end thereof connected via a pump 31 is provided. A lower stage of the main body 21 is formed in an empty aeration chamber 25, and a blower 26 is detachably attached to one side of the aeration chamber 25 so that a blower port 27 of the blower 26 faces the aeration chamber 25. A water supply pipe 29 for supplying treated water to an appropriate place is connected to a water outlet 28 opened at the bottom of the main body 21, and an exhaust port 3 is provided at the top of the main body 21.
It is configured by opening 0. Therefore, according to the aquaculture water treatment apparatus shown in the third embodiment, even if the heated water obtained by the water heating treatment apparatus 1 is high temperature sterilized water, the heat exchange action in the cooling chamber 23 is performed. Therefore, the water temperature can be adjusted so that the water temperature is appropriate for aquaculture (for example, 15 ° C. to 20 ° C.), or the amount of dissolved oxygen decreased in the water heat treatment apparatus 1, for example, about 4.5 to 6.5 mg / L is aerated. Dissolved oxygen amount of raw water, for example, 7.5 to 9.5 mg / L
It can be replenished to a certain level to make it optimal as aquaculture water for aquatic products.

【0018】図4に示されたものは、水加熱処理装置1
と空冷曝気装置20との間に保熱滅菌層16を配設して
水加熱処理装置1により得られた高温或いは低温の無菌
状の加熱水を、さらに保熱状態のもとで滅菌し、得られ
た処理水を空冷曝気装置20において養殖最適水温とな
るように調整せしめると同時に、水産生物の生息に必要
な溶存酸素量を含んだ養殖水を量産することができる水
産養殖水の処理装置の第4実施例を示すものであり、水
加熱処理装置1と保熱滅菌槽16とは三方弁13を備え
た通水管12で接続し、又保熱滅菌槽16と空冷曝気装
置20とは、一端が保熱滅菌槽16に接続され、他側が
空冷曝気装置20の散水器24に接続され、しかも、そ
の途中にポンプ33を設けた通水管32により接続され
ている。
FIG. 4 shows a water heat treatment apparatus 1
The heat-retaining sterilization layer 16 is disposed between the air-cooling and aerating device 20 and the high-temperature or low-temperature aseptic heated water obtained by the water heat treatment device 1 is further sterilized under a heat-retaining state, An aquaculture water treatment device capable of adjusting the obtained treated water in the air-cooling aeration device 20 so as to reach the optimum aquaculture water temperature and mass-producing the aquaculture water containing the dissolved oxygen amount necessary for inhabiting aquatic products. 4 shows a fourth embodiment of the present invention, in which the water heat treatment apparatus 1 and the heat retention sterilization tank 16 are connected by a water pipe 12 equipped with a three-way valve 13, and the heat retention sterilization tank 16 and the air-cooled aeration apparatus 20 are connected. , One end is connected to the heat retention sterilization tank 16, the other side is connected to the sprinkler 24 of the air-cooling aeration device 20, and is further connected by a water pipe 32 in which a pump 33 is provided.

【0019】[0019]

【発明の効果】本発明は、以上説明したような方法およ
び装置を有するので、以下に記載されるような効果を奏
する。流下する原水に、焔上する燃焼ガスを直接接触さ
せて加熱水を得るようにしたので、加熱水は完全に殺菌
された無菌状態となり、水産生物の養殖水として有効的
に使用することができる。そして、水加熱処理装置によ
り得られた加熱水は通水管を介し保熱滅菌槽へ収容して
所定時間保熱状態を維持させたので、たとえ加熱水温が
比較的低温であった場合においても、滅菌効果をより一
層促進せしめてミズカビ病等の発生を未然に防止し、水
産生物の養殖水として有効的に提供することができる。
その上、水加熱処理装置或いは保熱滅菌槽において処理
された滅菌状態の加熱水は空冷曝気装置に供給され、空
冷曝気されたので、加熱水がたとえ高温のものであって
も、加熱水を養殖に最適な水温に調整管理することがで
きる許りか、加熱水の溶存酸素量を原水の溶存酸素量の
水準まで補給せしめ、水産生物の養殖をより効果的なら
しめ、もって、簡単な方法および装置により有益な養殖
水を短時間のもとに量産して提供することができる。な
お、細菌検査成績の一例を示せば下表の通りである。
Since the present invention has the method and apparatus described above, it has the following effects. The raw water that flows down is directly contacted with the combustion gas that rises to obtain heated water, so the heated water becomes completely sterilized and can be effectively used as aquaculture water for aquatic products. . Then, since the heated water obtained by the water heat treatment device was stored in the heat-retaining sterilization tank through the water passage to maintain the heat-retention state for a predetermined time, even when the heated water temperature was relatively low, It is possible to further promote the sterilization effect to prevent the occurrence of mold fungus and the like, and to effectively provide the aquatic product as aquaculture water.
Moreover, the sterilized heated water treated in the water heat treatment device or the heat-retaining sterilization tank is supplied to the air-cooling aeration device and aerated by air-cooling. Permitting that the water temperature can be adjusted and controlled optimally for aquaculture, the dissolved oxygen content of the heated water can be replenished to the level of the dissolved oxygen content of the raw water, making the aquaculture of aquatic products more effective. The device can mass-produce useful aquaculture water in a short time and provide it. The table below shows an example of the bacterial test results.

【表1】 [Table 1]

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

【図1】一部を切欠し、要部を破断した第1実施例に係
る水産養殖水の処理装置の正面図である。
FIG. 1 is a front view of an aquaculture water treatment device according to a first embodiment with a part cut away and a main part broken.

【図2】一部を切欠し、要部を破断した第2実施例に係
る水産養殖水の処理装置の正面図である。
FIG. 2 is a front view of the aquaculture water treatment device according to the second embodiment with a part cut away and a main part broken.

【図3】一部を切欠し、要部を破断した第3実施例に係
る水産養殖水の処理装置の正面図である。
FIG. 3 is a front view of the aquaculture water treatment device according to the third embodiment with a part cut away and a main part broken.

【図4】一部を切欠し、要部を破断した第4実施例に係
る水産養殖水の処理装置の正面図である。
FIG. 4 is a front view of the aquaculture water treatment device according to the fourth embodiment with a part cut away and a main part broken.

【符号の説明】[Explanation of symbols]

1 水加熱処理装置 2 本体 3 熱交換層 4 燃交換室 5 散水器 8 燃焼室 9 バーナ 10 燃焼口 12 通水管 16 保熱滅菌槽 17 保温材 20 空冷曝気装置 21 本体 22 熱交換層 23 冷却室 24 散水器 25 曝気室 26 送風機 27 送風口 1 Water Heat Treatment Device 2 Main Body 3 Heat Exchange Layer 4 Combustion Exchange Room 5 Sprinkler 8 Combustion Chamber 9 Burner 10 Combustion Port 12 Water Pipe 16 Heat-Retaining Sterilizer 17 Heat-Retaining Material 20 Air-cooling Aerator 21 Main Body 22 Heat-Exchange Layer 23 Cooling Room 24 Sprinkler 25 Aeration chamber 26 Blower 27 Blower

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 流下する原水に、焔上する燃焼ガスを直
接接触させて加熱し、加熱殺菌された養殖水としたこと
を特徴とする水産養殖水の処理方法。
1. A method for treating aquaculture water, wherein the raw water that flows down is directly brought into contact with a combustion gas that is to be heated and heated to obtain heat-sterilized culture water.
【請求項2】 流下する原水に、焔上する燃焼ガスを直
接接触させて加熱し、得られた加熱水を一旦保熱滅菌槽
へ収容して滅菌処理したことを特徴とする水産養殖水の
処理方法。
2. Aquaculture water characterized in that the raw water flowing down is directly brought into contact with heating combustion gas for heating, and the resulting heated water is once stored in a heat retention sterilization tank and sterilized. Processing method.
【請求項3】 流下する原水に、焔上する燃焼ガスを直
接接触させて加熱し、得られた加熱水を流通する空気と
直接接触するよう流下せしめて空冷曝気したことを特徴
とする水産養殖水の処理方法。
3. An aquaculture characterized by air-cooling and aeration, wherein the raw water flowing down is directly brought into contact with a combustion gas that has risen to heat it, and the resulting heated water is allowed to flow down so as to come into direct contact with the circulating air. Water treatment method.
【請求項4】 本体内の上段に散水器および熱交換層を
設けた熱交換室を、下段にバーナの燃焼口を臨ませた燃
焼室を立体的に配設した水加熱処理装置と、周囲を保温
加工した保熱滅菌槽とを通水管を介し接続したことを特
徴とする水産養殖水の処理装置。
4. A water heat treatment device in which a heat exchange chamber having a water sprinkler and a heat exchange layer is provided in an upper stage of the main body, and a combustion chamber facing a combustion port of a burner is three-dimensionally disposed in a lower stage, and a surrounding area. An aquaculture water treatment device, characterized in that it is connected to a heat-retaining sterilization tank that has been heat-insulated via a water pipe.
【請求項5】 本体内の上段に散水器および熱交換層を
設けた熱交換室を、下段にバーナの燃焼口を臨ませた燃
焼室を立体的に配設した水加熱処理装置と、本体内の上
段に散水器および熱交換層を設けた冷却室を、下段に送
風機の送風口を臨ませた曝気室を設けた空冷曝気装置と
を通水管を介し接続したことを特徴とする水産養殖水の
処理装置。
5. A water heat treatment apparatus in which a heat exchange chamber having a water sprinkler and a heat exchange layer provided in an upper stage of the main body and a combustion chamber having a combustion port of a burner in a lower stage are three-dimensionally arranged, and a main body. An aquaculture characterized by connecting a cooling chamber with a sprinkler and a heat exchange layer in the upper part of the inside to an air-cooling aeration device with an aeration chamber facing the blower opening of the blower through a water pipe. Water treatment equipment.
【請求項6】 水加熱処理装置と空冷曝気装置との間に
保熱滅菌槽を配設したことを特徴とする請求項5記載の
水産養殖水の処理装置。
6. The treatment apparatus for aquaculture water according to claim 5, wherein a heat-retaining sterilization tank is provided between the water heating treatment apparatus and the air-cooling aeration apparatus.
【請求項7】 水加熱処理装置と空冷曝気装置との間に
配設した保熱滅菌槽の給水側は水加熱処理装置の燃焼室
に、また排水側は空冷曝気装置の散水器にそれぞれ接続
したことを特徴とする請求項5または請求項6記載の水
産養殖水の処理装置。
7. The water supply side of the heat retention sterilization tank disposed between the water heating treatment device and the air cooling aeration device is connected to the combustion chamber of the water heating treatment device, and the drain side is connected to the sprinkler of the air cooling aeration device. The aquaculture water treatment apparatus according to claim 5 or 6, wherein
JP18181991A 1991-06-26 1991-06-26 Method and apparatus for treating aquaculture water Expired - Fee Related JPH0824511B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18181991A JPH0824511B2 (en) 1991-06-26 1991-06-26 Method and apparatus for treating aquaculture water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18181991A JPH0824511B2 (en) 1991-06-26 1991-06-26 Method and apparatus for treating aquaculture water

Publications (2)

Publication Number Publication Date
JPH053736A JPH053736A (en) 1993-01-14
JPH0824511B2 true JPH0824511B2 (en) 1996-03-13

Family

ID=16107381

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18181991A Expired - Fee Related JPH0824511B2 (en) 1991-06-26 1991-06-26 Method and apparatus for treating aquaculture water

Country Status (1)

Country Link
JP (1) JPH0824511B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6059922A (en) * 1996-11-08 2000-05-09 Kabushiki Kaisha Toshiba Plasma processing apparatus and a plasma processing method
JP2008157673A (en) * 2006-12-21 2008-07-10 Sii Nanotechnology Inc Method for forming grasping surface of sample grasping member

Also Published As

Publication number Publication date
JPH053736A (en) 1993-01-14

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