JPH04104748A - Device for cleaning fish-culturing water - Google Patents

Device for cleaning fish-culturing water

Info

Publication number
JPH04104748A
JPH04104748A JP2218099A JP21809990A JPH04104748A JP H04104748 A JPH04104748 A JP H04104748A JP 2218099 A JP2218099 A JP 2218099A JP 21809990 A JP21809990 A JP 21809990A JP H04104748 A JPH04104748 A JP H04104748A
Authority
JP
Japan
Prior art keywords
water
tank
pipe
fish
valve
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
JP2218099A
Other languages
Japanese (ja)
Inventor
Masahiko Tsutsumi
正彦 堤
Kyozo Kawachi
河内 恭三
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP2218099A priority Critical patent/JPH04104748A/en
Publication of JPH04104748A publication Critical patent/JPH04104748A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PURPOSE:To provide the subject device capable of effectively cleaning supply water, preventing fishes and shellfish from diseases caused by pathogenic bacteria and fungi and accelerating the good growth of the fishes and shellfish by disposing an organic substance, solid substance-removing means and a pressure- driven separation membrane means in a line for supplying water in a fish culture tank. CONSTITUTION:In the objective device, a biomembrane treating tank 20 comprising a tapered portion 21 and a cylinder portion 22 having a filter bed (e.g. a filter material comprising activated carbon or the like) disposed between an upper support member 24 and a lower support member 25 and a pressure- driven separation membrane means 65 comprising an ultrafiltration membrane and connected to pipes 50, 52, 54, 56, 58 and 60 from the inside of an oxygen- dissolving tank 40 are disposed in a line for the supply water 130 of a fish culture tank 90.

Description

【発明の詳細な説明】 [発明の目的コ (産業上の利用分野) この発明は、魚介類を飼育するための養魚槽、池等に対
する補給水を浄化するための養魚水浄化装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Purpose of the Invention (Field of Industrial Application) This invention relates to a fish farming water purification device for purifying supply water for fish tanks, ponds, etc. for raising fish and shellfish.

(従来の技術) 例えば廃水、下水処理場等の水処理施設で得られる処理
水により魚介類を飼育するための養魚槽、池等で補給水
を浄化するためのに用いられる養魚水浄化装置として、
従来、第2図に示すようなものが知られている。
(Prior art) For example, as a fish water purification device used to purify supplementary water in fish tanks, ponds, etc. for raising fish and shellfish using treated water obtained from water treatment facilities such as wastewater and sewage treatment plants. ,
Conventionally, a device as shown in FIG. 2 has been known.

この従来の養魚水浄化装置は、補給水1を生物膜処理槽
2に供給して補給水1に含まれている有機物・固形物を
除去し、さらに酸素溶解槽3に供給して散気管4から送
り込まれる気泡5と接触させることにより溶存酸素濃度
(DO)を飽和付近まで上昇させておき、養魚槽6内の
水位の低下に応して、この酸素溶解槽3内の水を養魚$
116に補給する構成である。そして、養魚槽6内の水
に対しては、生物膜処理槽7に供給することにより魚の
排泄物や病原菌等の汚染物質を減少させ、さらに酸素溶
解槽9に供給してDOを上昇させ、これをポンプ10に
より再び養魚P!6に返送するようにして、循環浄化を
行うようにしている。なお、開閉弁11は養魚槽6の底
部に蓄積した汚泥を排出するためのものであり、12は
溢流水である。
This conventional fish farming water purification device supplies make-up water 1 to a biofilm treatment tank 2 to remove organic matter and solid matter contained in the make-up water 1, and then supplies it to an oxygen dissolution tank 3 to remove the organic matter and solid matter contained in the make-up water 1. The dissolved oxygen concentration (DO) is raised to near saturation by bringing it into contact with air bubbles 5 sent from
116. The water in the fish culture tank 6 is supplied to a biofilm treatment tank 7 to reduce contaminants such as fish excrement and pathogenic bacteria, and further supplied to an oxygen dissolution tank 9 to increase DO. The pump 10 is used for fish farming P! 6, to perform cyclical purification. Note that the on-off valve 11 is for discharging sludge accumulated at the bottom of the fish culture tank 6, and 12 is overflow water.

(発明が解決しようとする課題) しかしながら、このような従来の養魚水浄化装置では、
補給水1の中に大腸菌、かび類等の病原菌や病害虫、さ
らには病害虫卵等が存在した場合、生物膜処理槽2にお
いては除去できず、酸素溶解槽3内の曝気によって増殖
し、養魚槽6に供給されるので、養魚槽6内の魚8が病
原菌や病害虫によって汚染され、病気にかかって死滅す
ることがあるという問題点があった。
(Problem to be solved by the invention) However, in such a conventional fish farming water purification device,
If pathogenic bacteria such as Escherichia coli, mold, pests, or even eggs of pests are present in the supplementary water 1, they cannot be removed in the biofilm treatment tank 2, and they proliferate due to the aeration in the oxygen dissolution tank 3. There is a problem in that the fish 8 in the fish culture tank 6 are contaminated with pathogenic bacteria and pests, and may become infected and die.

また養魚槽6内の病原菌や病害虫を除去するために、生
物膜処理槽7、酸素溶解槽9による循環浄化を行っても
、生物膜処理槽7では十分な除去てきないため、養魚槽
6内には病原菌や病害虫か増殖し、魚8が死滅すること
があるという問題点があった。
Furthermore, in order to remove pathogenic bacteria and pests in the fish culture tank 6, even if circulation purification is performed using the biofilm treatment tank 7 and the oxygen dissolution tank 9, the biofilm treatment tank 7 cannot remove the pathogens and pests sufficiently. However, there was a problem in that the fish 8 could die due to the proliferation of pathogenic bacteria and pests.

この発明は、このような従来の問題点に鑑みてなされた
もので、補給水中の病原菌や病害虫を除去してから養魚
槽に補給することによって養魚槽内の魚介類を正常に成
育させることかできるようにした養魚水浄化装置を提供
することを目的とする。
This invention was made in view of such conventional problems, and it is possible to make the fish and shellfish in the fish tank grow normally by removing pathogens and pests from the supply water and then replenishing the fish tank. The purpose of the present invention is to provide a fish farming water purification device that makes it possible to purify fish water.

[発明の構成] (課題を解決するための手段) この発明の養魚水浄化装置は、養魚槽の補給水ラインに
有機物・固形物除去を除去するための有機物・固形物除
去手段と、補給水中の細菌の滅菌を行うための圧力駆動
分離膜手段とを設けたものである。
[Structure of the Invention] (Means for Solving the Problem) The fish farming water purification device of the present invention includes an organic matter/solid matter removal means for removing organic matter/solid matter in the make-up water line of a fish tank, and a means for removing organic matter/solid matter in the make-up water line of the fish tank. and a pressure-driven separation membrane means for sterilizing bacteria.

(作用) この発明の養魚水浄化装置では、例えば生物膜処理手段
のような有機物・固形物除去手段によって補給水中の有
機物・固形物を除去し、続く圧力駆動分離膜手段によっ
て補給水中の病原菌や病害虫を分離除去し、圧力分離駆
動膜を透過した水を養魚槽に補給することにより、養魚
槽中の魚介類に安全な水を供給することができる。
(Function) In the fish farming water purification device of the present invention, organic matter and solid matter in the make-up water are removed by an organic matter and solid matter removal means such as a biofilm treatment means, and pathogenic bacteria and other substances in the make-up water are removed by a subsequent pressure-driven separation membrane means. By separating and removing pests and replenishing the fish tank with water that has passed through the pressure separation driven membrane, safe water can be supplied to the fish and shellfish in the fish tank.

(実施例) 以下、この発明の実施例を図に基づいて詳説する。(Example) Hereinafter, embodiments of the present invention will be explained in detail based on the drawings.

第1図はこの発明の一実施例であり、有機物・固形物除
去手段として生物膜処理槽を用い、圧力駆動分離膜手段
として限外ろ過膜(以下、UF膜と称する)を用いた養
魚水浄化装置の実施例を示している。
FIG. 1 shows an embodiment of the present invention, in which a biofilm treatment tank is used as the organic matter/solid matter removal means, and an ultrafiltration membrane (hereinafter referred to as UF membrane) is used as the pressure-driven separation membrane means. An example of a purification device is shown.

第1図において、20は生物膜処理槽、40は酸素溶解
槽、65はUF膜モジュール、90は養魚槽、100は
循環水用の生物膜処理槽、114は酸素溶解槽、120
は循環ポンプである。
In FIG. 1, 20 is a biofilm treatment tank, 40 is an oxygen dissolution tank, 65 is a UF membrane module, 90 is a fish culture tank, 100 is a biofilm treatment tank for circulating water, 114 is an oxygen dissolution tank, 120
is a circulation pump.

生物膜処理槽20は、逆円錐状のテーパ一部21と、円
筒部22とから形成されており、上部に溢流壁23か生
物膜処理槽20と同心状に配設され、上部支持部24と
下部支持部25との間には活性炭、砂、セラミ7クス等
のる材が充填されたろ床26が設けられ、下部間隙部2
7には散気管28が設けられている。この散気管28は
、開閉弁29を有する管30を介して空気源31と接続
されており、円筒部22の下部で下部間隙部27に該当
する部分の側面にポンプ32を有する管33が配設され
、またテーパ一部21の底部には開閉弁34を有する管
35が配設されている。溢流壁23に接続された管36
は、酸素溶解槽40の上部に溢流水を流下するようにな
っている。
The biofilm treatment tank 20 is formed of an inverted conical tapered part 21 and a cylindrical part 22, and an overflow wall 23 is disposed at the upper part concentrically with the biofilm treatment tank 20, and an upper support part A filter bed 26 filled with a material such as activated carbon, sand, and ceramic 7x is provided between the lower gap part 24 and the lower support part 25.
7 is provided with an aeration pipe 28. This diffuser pipe 28 is connected to an air source 31 via a pipe 30 having an on-off valve 29, and a pipe 33 having a pump 32 is arranged on the side surface of a portion corresponding to the lower gap 27 at the bottom of the cylindrical portion 22. A pipe 35 having an on-off valve 34 is disposed at the bottom of the tapered portion 21. Pipe 36 connected to overflow wall 23
The overflow water is made to flow down to the upper part of the oxygen dissolution tank 40.

酸素溶解槽40は、逆円錐状のテーパ一部41と、円筒
部42から形成されており、その下部に散気管43が設
けられている。この散気管43は開閉弁44を有する管
45を介して空気源31と接続され、酸素溶解槽40の
底部には開閉弁46を有する管47か接続されている。
The oxygen dissolving tank 40 is formed from an inverted conical tapered part 41 and a cylindrical part 42, and a diffuser pipe 43 is provided at the bottom thereof. This diffuser pipe 43 is connected to the air source 31 via a pipe 45 having an on-off valve 44, and a pipe 47 having an on-off valve 46 is connected to the bottom of the oxygen dissolving tank 40.

酸素溶解1’!40内には上限スイッチと下限スイッチ
を具備した水位計48が設けられ、これがレベルコント
ローラ49と電気的に接続されている。
Oxygen dissolution 1'! A water level gauge 48 having an upper limit switch and a lower limit switch is provided within the water level controller 40 and is electrically connected to a level controller 49 .

酸素溶解槽40の内部の水位計48の下限スイッチの位
置より下方で、かつ散気管43より上方の位置に管50
か設けられている。この管5oは、ポンプ51、管52
、連結部53、管54、開閉弁55、管56、連結部5
7、管58、捕集器59、管60を順に介してUF膜モ
ジュール65の入口側66に接続されている。UF膜モ
ジュール65の出口側67は管68、捕集器69、管7
0゜連結部71、管72、開閉弁73、管74、連結部
75、管76を順に介して酸素溶解槽4oの上部に接続
されている。
A pipe 50 is located below the lower limit switch position of the water level gauge 48 inside the oxygen dissolution tank 40 and above the aeration pipe 43.
Or is provided. This pipe 5o includes a pump 51 and a pipe 52.
, connecting portion 53, pipe 54, on-off valve 55, pipe 56, connecting portion 5
7, a pipe 58, a collector 59, and a pipe 60, which are connected to the inlet side 66 of the UF membrane module 65 in this order. The outlet side 67 of the UF membrane module 65 is connected to a pipe 68, a collector 69, and a pipe 7.
It is connected to the upper part of the oxygen dissolving tank 4o via a 0° connection part 71, a pipe 72, an on-off valve 73, a pipe 74, a connection part 75, and a pipe 76 in this order.

このUF膜モジュール65の部分にはスポンジボール7
7が設けられており、レベルコントローラ49の出力側
はポンプ51の入力側に電気的に接続され、連結部53
は開閉弁80を有する管81を介して連結部71と接続
され、連結部57は開閉弁82を有する管83を介して
連結部75と接続されている。
A sponge ball 7 is attached to this UF membrane module 65.
7, the output side of the level controller 49 is electrically connected to the input side of the pump 51, and the connecting part 53
is connected to the connecting portion 71 via a pipe 81 having an on-off valve 80, and the connecting portion 57 is connected to the connecting portion 75 via a pipe 83 having an on-off valve 82.

UF膜モジュール65の透過水出口側85に接続された
管86は、養魚槽90の上部に補給水を流下するように
なっている。
A pipe 86 connected to the permeated water outlet side 85 of the UF membrane module 65 is configured to flow make-up water to the upper part of the fish culture tank 90.

養魚槽90の上部には溢流壁91が設けられており、こ
の溢流壁91は管92と接続されており、養魚槽90の
底部には開閉弁93を有する管94が接続されている。
An overflow wall 91 is provided at the top of the fish culture tank 90, and this overflow wall 91 is connected to a pipe 92, and a pipe 94 having an on-off valve 93 is connected to the bottom of the fish culture tank 90. .

また養魚槽90の側面部にポンプ95を有する管96が
設けられ、管96は生物膜処理槽100の下方側面部に
接続されている。
Further, a pipe 96 having a pump 95 is provided on the side surface of the fish culture tank 90, and the pipe 96 is connected to the lower side surface of the biofilm treatment tank 100.

生物膜処理槽100は、上方の円筒部101と下方のテ
ーパ一部102から形成され、上部支持部103と、下
部支持部104との間にろ材が充填されたろ床105が
設けられており、下部間隙部106内には散気管107
か配設されている。
The biofilm treatment tank 100 is formed from an upper cylindrical part 101 and a lower tapered part 102, and a filter bed 105 filled with a filter material is provided between an upper support part 103 and a lower support part 104. A diffuser pipe 107 is provided in the lower gap 106.
or has been set up.

この散気管107は、開閉弁108を有する管109を
介して空気源31に接続されており、生物膜処理槽10
0の底部には開閉弁110を有する管111が接続され
ている。
This aeration pipe 107 is connected to the air source 31 via a pipe 109 having an on-off valve 108, and is connected to the biofilm treatment tank 10.
A pipe 111 having an on-off valve 110 is connected to the bottom of the 0.

生物膜処理槽100の上部に配した溢流壁112は、管
113を介して酸素溶解槽1114の上部に接続されて
いる。
An overflow wall 112 disposed at the top of the biofilm treatment tank 100 is connected to the top of an oxygen dissolution tank 1114 via a pipe 113.

酸素溶解槽114は、円筒部115とテーパー部116
から形成され、酸素溶解槽114内下部には散気管11
7が配設され、この散気管117は開閉弁118を有す
る管119を介して空気源31と接続されている。また
酸素溶解槽114内の下部は、ポンプ120を有する管
121を介して養魚槽90の上部に接続されていて、処
理済みの養魚水を養魚槽90に返送するようになってい
る。
The oxygen dissolution tank 114 has a cylindrical portion 115 and a tapered portion 116.
The oxygen dissolving tank 114 has a diffuser pipe 11 in the lower part thereof.
7 is provided, and this diffuser pipe 117 is connected to the air source 31 via a pipe 119 having an on-off valve 118. The lower part of the oxygen dissolution tank 114 is connected to the upper part of the fish tank 90 via a pipe 121 having a pump 120, so that the treated fish water is returned to the fish tank 90.

次に、上記の構成の養魚水浄化装置の動作について説明
する。
Next, the operation of the fish farming water purification device having the above configuration will be explained.

この実施例の養魚水浄化装置は、(1)補給水浄化運転
、(2)UF膜洗浄運転、(3)補給水ラインの生物膜
処理槽洗浄運転、(4)養魚水浄化運転、(5)循環ラ
インの生物膜処理槽洗浄運転、の5つの運転を行うこと
ができる。
The fish farming water purification device of this embodiment includes (1) makeup water purification operation, (2) UF membrane cleaning operation, (3) makeup water line biofilm treatment tank cleaning operation, (4) fish farming water purification operation, (5) ) A biofilm treatment tank cleaning operation of the circulation line can be performed.

(1)補給水浄化運転 すべての開閉弁を閉し、ポンプ32を作動して補給水1
30を生物膜処理120に供給する。
(1) Make-up water purification operation Close all on-off valves, operate the pump 32, and clean the make-up water 1.
30 to biofilm treatment 120.

補給水130は下部間隙部27、下部支持部25、ろ床
26、上部支持部24を順次介して上昇する。
The makeup water 130 ascends through the lower gap 27, the lower support 25, the filter bed 26, and the upper support 24 in this order.

ろ床26を通過する過程において、補給水130内の固
形物がろ床26内のる材に付着、吸着され、また有機物
はる床26内のろ材表面に形成された生物膜によって分
解除去される。
In the process of passing through the filter bed 26, the solids in the make-up water 130 are attached and adsorbed to the material in the filter bed 26, and the organic matter is decomposed and removed by the biofilm formed on the surface of the filter material in the bed 26. Ru.

このように有機物・固形物が減少した水は、溢流壁23
から管36を介して酸素溶解槽40に供給される。
The water with reduced organic matter and solid matter flows through the overflow wall 23.
The oxygen is supplied to the oxygen dissolution tank 40 via a pipe 36.

酸素溶解槽40内に供給された水の液面が上昇し、水位
計48の上限スイッチまで達するとポンプ32を停止し
、開閉弁44を開いてエアを酸素溶解槽40内に吹き込
む。そして、数分間曝気して、酸素溶解槽40内の水の
Doを上昇させた後、開閉弁44を閉しる。
When the liquid level of the water supplied into the oxygen dissolving tank 40 rises and reaches the upper limit switch of the water level gauge 48, the pump 32 is stopped, the on-off valve 44 is opened, and air is blown into the oxygen dissolving tank 40. Then, after aeration is carried out for several minutes to raise Do of the water in the oxygen dissolving tank 40, the on-off valve 44 is closed.

次に、開閉弁55と開閉弁73とを開き、ポンプ51を
作動させてUF膜運転を行う。つまり、酸素溶解槽40
内の水を管50、ポンプ51、管52、連結部53、管
54、開閉弁55、管56、連結部57、管58、捕集
器59、管60を順次介してUF膜モンユール65の入
口側66に供給する。
Next, the on-off valve 55 and the on-off valve 73 are opened, and the pump 51 is operated to perform UF membrane operation. In other words, the oxygen dissolution tank 40
The water inside is passed through the pipe 50, pump 51, pipe 52, connecting part 53, pipe 54, on-off valve 55, pipe 56, connecting part 57, pipe 58, collector 59, and pipe 60 in order to the UF membrane Moneur 65. The inlet side 66 is supplied.

そして、この水はUF膜モジュール65内を通過して出
口側から管68、捕集器69、管70、連結部71、管
72、開閉弁73、管74、連結部75、管76を順次
介して酸素溶解槽40へ返送され、循環する。
Then, this water passes through the UF membrane module 65 and sequentially passes through the pipe 68, collector 69, pipe 70, connection part 71, pipe 72, on-off valve 73, pipe 74, connection part 75, and pipe 76 from the outlet side. The oxygen is returned to the oxygen dissolution tank 40 through the oxygen dissolution tank 40 and circulated therein.

酸素溶解槽40内の大腸菌、かび類等の病原菌や病害虫
はUF膜モノュール65のUF膜を透過できず、補給水
の一部か病原菌や病害虫を完全除去されてUF膜を透過
して透過水出口側85から管86を介して養魚槽90の
上部に補給される。
Pathogens and pests such as Escherichia coli and mold in the oxygen dissolution tank 40 cannot pass through the UF membrane of the UF membrane monole 65, and some of the make-up water passes through the UF membrane with the pathogens and pests completely removed. The upper part of the fish tank 90 is replenished from the outlet side 85 via a pipe 86.

除菌水を養魚槽90に供給する量、つまり、UF膜の透
過量分たけ酸素溶解槽40内の液面か減少し、液面が水
位計48の下限スイッチまで到達すると、ポンプ51を
停止する。そして、次に、前記と同様にポンプ32を作
動させて補給水130を生物膜処理槽20に供給し、以
上の操作を繰り返すことにより、補給水130の浄化、
除菌を行うのである。
When the amount of sterilized water supplied to the fish culture tank 90, that is, the liquid level in the oxygen dissolving tank 40 decreases by the amount of permeation through the UF membrane, and the liquid level reaches the lower limit switch of the water level gauge 48, the pump 51 is stopped. do. Then, the pump 32 is operated in the same manner as described above to supply the make-up water 130 to the biofilm treatment tank 20, and the above operations are repeated to purify the make-up water 130.
It is sterilization.

(2)UF膜洗浄運転 この運転は、UF膜モジュール65による補給水浄化運
転を行うと、UF膜表面に汚物のケーキ層が形成される
が、これをスポンジボール77を用いて剥離、洗浄する
目的で行われ、1日に1〜10回の開度で、次の操作に
従って行われる。
(2) UF membrane cleaning operation In this operation, when the make-up water purification operation is performed using the UF membrane module 65, a cake layer of dirt is formed on the surface of the UF membrane, but this is peeled off and cleaned using the sponge ball 77. It is carried out according to the following operations, with openings from 1 to 10 times a day.

酸素溶解槽40内の液面が水位計48の上限スイッチま
で達して上限スイッチがオンとなった時、、開閉弁55
と開閉弁73を閉し、開閉弁80と開閉弁82を開き、
ポンプ51を作動する。
When the liquid level in the oxygen dissolution tank 40 reaches the upper limit switch of the water level gauge 48 and the upper limit switch is turned on, the on-off valve 55
and close the on-off valve 73, open the on-off valve 80 and the on-off valve 82,
Activate the pump 51.

この操作により、酸素溶解槽40内の水は1点鎖線aで
示すように、管50、ポンプ51、管52、連結部53
、管81、開閉弁80、連結部71、管70、捕集器6
9、管68、出口側67、UF膜モジュール65、入口
側66、管60、捕集器59、管58、連結部57、管
83、開閉弁82、連結部75、管76を順次介して元
の酸素溶解槽40に返送する。この操作により、UF膜
モジュール65の内部で補給水浄化運転の時とは流れが
逆転し、捕集器69にあったスポンジボール77がUF
膜モジュール65内を通過する過程において、UF膜表
面に形成したケーキ層を剥離させる。
With this operation, the water in the oxygen dissolution tank 40 is transferred to the pipe 50, pump 51, pipe 52, and connecting portion 53 as shown by the dashed line a.
, pipe 81, on-off valve 80, connecting part 71, pipe 70, collector 6
9, the pipe 68, the outlet side 67, the UF membrane module 65, the inlet side 66, the pipe 60, the collector 59, the pipe 58, the connecting part 57, the pipe 83, the on-off valve 82, the connecting part 75, and the pipe 76 in order. It is returned to the original oxygen dissolution tank 40. By this operation, the flow inside the UF membrane module 65 is reversed from that during the make-up water purification operation, and the sponge balls 77 in the collector 69 become UF.
In the process of passing through the membrane module 65, the cake layer formed on the surface of the UF membrane is peeled off.

次に、ポンプ51を停止して開閉弁80と開閉弁82を
閉じた後、開閉弁55と開閉弁73を開いてポンプ51
を作動させ、流れを元のように逆転させ、スポンジボー
ル77をUF膜モジュール65内を捕集器59から捕集
器69側へ通過させる。
Next, after stopping the pump 51 and closing the on-off valve 80 and the on-off valve 82, the on-off valve 55 and the on-off valve 73 are opened and the pump 51 is closed.
is activated, the flow is reversed to the original state, and the sponge balls 77 are passed through the UF membrane module 65 from the collector 59 to the collector 69 side.

この操作を5〜10回繰り返すことにより、スポンジボ
ール77かUF膜モジュール65の内部を通過する旅に
UF膜の表面のケーキ層を剥離させ、UF膜を再生させ
ることができる。
By repeating this operation 5 to 10 times, the cake layer on the surface of the UF membrane can be peeled off as the sponge ball 77 passes through the inside of the UF membrane module 65, and the UF membrane can be regenerated.

(3)補給水ラインの生物膜処理槽洗浄運転この運転は
、前記(1)の補給水浄化運転で生物膜処理槽20内の
ろ床26のろ材表面に過剰に付着した生物膜を強制剥離
する運転であり、1週間に1〜7回の開度で次の操作に
よって行う。
(3) Biofilm treatment tank cleaning operation of makeup water line This operation forcibly removes the biofilm excessively attached to the surface of the filter media of the filter bed 26 in the biofilm treatment tank 20 in the makeup water purification operation of (1) above. This operation is performed by the following operation at an opening degree of 1 to 7 times a week.

すべての開閉弁を閉じ、ポンプ32を作動させて補給水
130を生物膜処理槽20に供給し、溢流壁23から溢
流させる。溢流したなら、開閉弁34を開いて液面を溢
流壁23より下方で、かつ上部支持部24より上方の位
置にする。
All on-off valves are closed, and the pump 32 is operated to supply makeup water 130 to the biofilm treatment tank 20 and overflow from the overflow wall 23. If an overflow occurs, the on-off valve 34 is opened to bring the liquid level below the overflow wall 23 and above the upper support portion 24.

次に、開閉弁2つを開いてエアを生物膜処理槽20内に
供給し、1〜10分間曝気し、ろ床26のろ材表面に過
剰に付着した生物膜をエアのせん断力によって強制剥離
させる。続いて、開閉弁29を閉してエアの供給を停止
し、開閉弁34を開いて剥離生物膜を管35を介して排
泥する。
Next, open the two on-off valves to supply air into the biofilm treatment tank 20, and aerate for 1 to 10 minutes to forcibly peel off the biofilm excessively attached to the surface of the filter medium of the filter bed 26 by the shearing force of the air. let Subsequently, the on-off valve 29 is closed to stop the air supply, and the on-off valve 34 is opened to drain the detached biofilm through the pipe 35.

排泥後は、開閉弁34を閉してポンプ32を作動させ、
前記(1)の補給水浄化運転に移行する。
After removing mud, close the on-off valve 34 and operate the pump 32,
Shift to the make-up water purification operation in (1) above.

(4)養魚水浄化運転 この運転は、養魚槽90内の養魚水に含まれている有機
物・固形物を除去するためのものであり、前記(1)の
補給水浄化運転と並行して同時に行われる。
(4) Fish culture water purification operation This operation is to remove organic matter and solid matter contained in the fish culture water in the fish culture tank 90, and is performed simultaneously in parallel with the make-up water purification operation in (1) above. It will be done.

まず、開閉弁93,108,110,118をすべて閉
じ、ポンプ95を作動させて養魚槽90の水を管96を
介して生物膜処理槽100に供給する。養魚水は、下部
間隙部106、下部支持部104、ろ床105、上部支
持部103を順次介して溢流壁112まで達する。この
ろ床105を養魚水が通過する過程において、養魚水中
の有機物・固形物はろ床105のる材表面に付着した生
物膜によって分解・吸着される。
First, all the on-off valves 93, 108, 110, and 118 are closed, and the pump 95 is operated to supply water from the fish tank 90 to the biofilm treatment tank 100 via the pipe 96. The fish farming water reaches the overflow wall 112 via the lower gap 106, the lower support 104, the filter bed 105, and the upper support 103 in this order. In the process of the fish farming water passing through the filter bed 105, organic matter and solid matter in the fish farming water are decomposed and adsorbed by the biofilm attached to the surface of the material on which the filter bed 105 is covered.

これらの汚染物質が除去された水は、管113を介して
酸素溶解槽114に供給される。ここで開閉弁118を
開いてエアを酸素溶解槽114に供給し、酸素溶解槽1
14内の水のDoを飽和濃度近くまで上昇させる。
Water from which these contaminants have been removed is supplied to an oxygen dissolution tank 114 via a pipe 113. Here, the on-off valve 118 is opened to supply air to the oxygen dissolving tank 114, and the oxygen dissolving tank 1
The Do of water in 14 is raised to near the saturation concentration.

液面が上昇したなら、ポンプ120を作動させて酸素溶
解槽114内部の水を管121を介して養魚槽90に返
送し、循環浄化する。
When the liquid level rises, the pump 120 is activated to return the water inside the oxygen dissolution tank 114 to the fish culture tank 90 via the pipe 121 for circulation purification.

なおここで、ポンプ120の流速はポンプ95のものよ
り若干遅く設定し、酸素溶解槽114内に養魚水が十分
長時間滞留して酸素供給を受けるようにする。
Here, the flow rate of the pump 120 is set to be slightly slower than that of the pump 95 so that the fish culture water stays in the oxygen dissolution tank 114 for a sufficiently long time and receives oxygen supply.

(5)循環水ラインの生物膜処理槽洗浄運転この運転は
、前記(3)の補給水ラインの生物膜処理槽洗浄運転と
まったく同じ方法であり、生物膜処理槽100内のろ床
105のろ材表面に過剰に付着した生物膜を強制剥離す
る。この運転は、1週間に1〜7回の頻度で行う。
(5) Circulating water line biofilm treatment tank cleaning operation This operation is exactly the same as the makeup water line biofilm treatment tank cleaning operation in (3) above, and the filter bed 105 in the biofilm treatment tank 100 is Forcibly removes the biofilm that is excessively attached to the surface of the filter media. This operation is performed 1 to 7 times a week.

このようにして、この養魚水浄化装置では、補給水13
0に対して生物膜処理槽20において有機物・固形物を
生物処理によって除去し、さらに酸素溶解槽40におい
てDoを高くしてUF膜モジュール65に導き、ここで
病原菌や病害虫、さらに病害虫卵を除去し、こうして清
澄で、かつ除菌された水を養魚槽90に補給することが
できるようになる。
In this way, in this fish farming water purification device, the make-up water 13
0, organic matter and solid matter are removed by biological treatment in the biofilm treatment tank 20, and Do is further increased in the oxygen dissolution tank 40 and guided to the UF membrane module 65, where pathogenic bacteria, pests, and eggs of pests are removed. However, the fish culture tank 90 can be replenished with clear and sterilized water.

なお、上記の実施例では圧力駆動分離膜手段としてUF
膜モジュールを用いたが、UF膜モジュルの場合には、
透過フラックスが大きく、除菌水を多量に養魚槽に供給
することができる。また、生物膜処理手段に固定床式の
生物膜処理槽を用いたことにより、補給水の中の有機物
・固形物を同時に効率的に除去することができる。さら
に、生物膜処理槽内のろ床の逆洗装置に散気管から吹き
込むエアによる逆洗を行うようにしているので、ろ床の
ろ材表面に過剰に付着した生物膜を迅速に剥離除去する
ことができる。
In the above embodiment, UF is used as the pressure-driven separation membrane means.
Although a membrane module was used, in the case of a UF membrane module,
The permeation flux is large and a large amount of sterilized water can be supplied to the fish tank. Further, by using a fixed bed type biofilm treatment tank as the biofilm treatment means, organic matter and solid matter in the make-up water can be efficiently removed at the same time. Furthermore, the backwashing device for the filter bed in the biofilm treatment tank uses air blown from the aeration pipe to quickly peel off and remove excess biofilm that has adhered to the surface of the filter media in the filter bed. I can do it.

さらに、生物膜処理槽内に曝気装置を組み込んでいるた
めに、除菌水のDoが高く維持てき、養魚槽内の魚介類
を正常に飼育することができる。
Furthermore, since an aeration device is built into the biofilm treatment tank, the Do of the sterilized water can be maintained at a high level, allowing the fish and shellfish in the fish tank to be raised normally.

加えて、UF膜モジュールの洗浄にスポンジボールを用
いることにより、簡単な開閉弁の開閉操作のみで迅速に
洗浄を行うことができる。
In addition, by using a sponge ball to clean the UF membrane module, cleaning can be performed quickly by simply opening and closing the on-off valve.

なお、この発明は上記の実施例に限定されることはなく
、とくに圧力駆動分離膜手段としては、UF膜に代えて
、中空子膜、逆浸透膜(RO膜)などの圧力駆動式のも
のを広く利用することができる。
Note that the present invention is not limited to the above embodiments, and in particular, as the pressure-driven separation membrane means, instead of the UF membrane, pressure-driven membranes such as hollow membranes and reverse osmosis membranes (RO membranes) may be used. can be widely used.

また有機物・固形物除去手段として、生物膜処理手段の
うち、固定床式の生物膜処理槽を用いているが、流動床
式、膨張床式、回転円盤式、散水ろ床等の生物膜を用い
る処理方法のいずれをも利用することができる。
Among biofilm treatment methods, a fixed bed type biofilm treatment tank is used as a means for removing organic matter and solid matter. Any of the processing methods used can be utilized.

さらに、圧力駆動分離膜手段と生物膜処理槽のそれぞれ
の個数は限定されることはなく、複数個の組み合わせで
あってもよい。
Further, the numbers of pressure-driven separation membrane means and biofilm treatment tanks are not limited, and a combination of a plurality of them may be used.

さらに加えて、圧力駆動分離膜と生物膜処理槽以外の既
存の処理方式を上記の各の実施例の養魚水浄化装置に組
み込むことも可能であり、例えばオゾン処理、UV殺菌
、凝集沈殿法などの化学的処理や、活性汚泥法等の生物
学的処理や沈殿池、ストレーナによる物理的処理法を組
み込むことができる。
In addition, it is also possible to incorporate existing treatment methods other than the pressure-driven separation membrane and biofilm treatment tank into the fish farming water purification apparatus of each of the above embodiments, such as ozone treatment, UV sterilization, coagulation sedimentation method, etc. Chemical treatment, biological treatment such as activated sludge, and physical treatment using sedimentation tanks and strainers can be incorporated.

[発明の効果コ 以上のようにこの発明によれば、養魚槽、池等に供給す
る補給水に対して有機物・固形物除去手段と共に圧力駆
動分離膜手段を設けて補給水中の病原菌、病害虫、病害
虫卵等を除去するようにしているので、補給水中の有機
物・固形物の除去と共に魚介類に致命的な影響を与える
病原菌や病害虫を物理的に除去し、きれいな水にして補
給することかでき、従来のように補給水中の病原菌や病
害虫に起因する病気によって魚介類を死滅させることが
なく、正常な成育を行うことができる。
[Effects of the Invention] As described above, according to the present invention, a pressure-driven separation membrane means is provided in addition to organic matter/solid matter removal means for make-up water supplied to fish tanks, ponds, etc., to remove pathogens, pests, and pests in the make-up water. Since we remove pest eggs, etc. from the replenishment water, we physically remove pathogens and pests that can have a fatal effect on fish and shellfish, as well as remove organic matter and solid matter from the replenishment water, making it possible to use clean water for replenishment. Unlike conventional methods, fish and shellfish are not killed by diseases caused by pathogenic bacteria or pests in the supply water, and can grow normally.

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

第1図はこの発明の一実施例の系統図、第2図は従来例
の系統図である。 20・・・生物膜処理槽 40・・・酸素溶解槽65・
・・圧力駆動分離膜手段
FIG. 1 is a system diagram of an embodiment of the present invention, and FIG. 2 is a system diagram of a conventional example. 20... Biofilm treatment tank 40... Oxygen dissolution tank 65.
・・Pressure driven separation membrane means

Claims (1)

【特許請求の範囲】[Claims] 養魚槽の補給水ラインに有機物・固形物除去を除去する
ための有機物・固形物除去手段と、補給水中の細菌の滅
菌を行うための圧力駆動分離膜手段とを設けて成る養魚
水浄化装置。
A fish farming water purification device comprising a make-up water line of a fish tank equipped with an organic matter/solid matter removal means for removing organic matter/solid matters, and a pressure-driven separation membrane means for sterilizing bacteria in the make-up water.
JP2218099A 1990-08-21 1990-08-21 Device for cleaning fish-culturing water Pending JPH04104748A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2218099A JPH04104748A (en) 1990-08-21 1990-08-21 Device for cleaning fish-culturing water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2218099A JPH04104748A (en) 1990-08-21 1990-08-21 Device for cleaning fish-culturing water

Publications (1)

Publication Number Publication Date
JPH04104748A true JPH04104748A (en) 1992-04-07

Family

ID=16714619

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2218099A Pending JPH04104748A (en) 1990-08-21 1990-08-21 Device for cleaning fish-culturing water

Country Status (1)

Country Link
JP (1) JPH04104748A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0647399A (en) * 1992-07-10 1994-02-22 Ebara Infilco Co Ltd Water purifying treatment method
CN102372403A (en) * 2011-10-11 2012-03-14 中国石油化工股份有限公司 Treatment process of oil-containing sewage in low-permeability oil field
CN105884135A (en) * 2016-05-19 2016-08-24 浙江工业大学 Polluted-river-network-source-water multi-carrier biomembrane and membrane drinking water treatment facility
JP2018143195A (en) * 2017-03-08 2018-09-20 国立大学法人 鹿児島大学 Aquatic life rearing system and aquatic life rearing method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0647399A (en) * 1992-07-10 1994-02-22 Ebara Infilco Co Ltd Water purifying treatment method
CN102372403A (en) * 2011-10-11 2012-03-14 中国石油化工股份有限公司 Treatment process of oil-containing sewage in low-permeability oil field
CN105884135A (en) * 2016-05-19 2016-08-24 浙江工业大学 Polluted-river-network-source-water multi-carrier biomembrane and membrane drinking water treatment facility
JP2018143195A (en) * 2017-03-08 2018-09-20 国立大学法人 鹿児島大学 Aquatic life rearing system and aquatic life rearing method

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