JPH1066963A - Pressure-type circulatory filter - Google Patents

Pressure-type circulatory filter

Info

Publication number
JPH1066963A
JPH1066963A JP9031538A JP3153897A JPH1066963A JP H1066963 A JPH1066963 A JP H1066963A JP 9031538 A JP9031538 A JP 9031538A JP 3153897 A JP3153897 A JP 3153897A JP H1066963 A JPH1066963 A JP H1066963A
Authority
JP
Japan
Prior art keywords
tank
filtration tank
liquid
pressure
physical
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
JP9031538A
Other languages
Japanese (ja)
Inventor
Kinya Kitagawa
欽哉 北川
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.)
Yamaha Motor Co Ltd
Original Assignee
Yamaha Motor 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 Yamaha Motor Co Ltd filed Critical Yamaha Motor Co Ltd
Priority to JP9031538A priority Critical patent/JPH1066963A/en
Publication of JPH1066963A publication Critical patent/JPH1066963A/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

PROBLEM TO BE SOLVED: To automatically remove the impurities such as body fluid of fish deposited on a bubble and floated along with the bubble by providing a closed part at the upper part of a bubble treating tank and furnishing a discharge means for removing the impurities outside the tank along with the bubbled liq. to the closed part. SOLUTION: A lid 6b formed from a transparent plastic and convexed upward is detachably fixed to the upper part of a bubble treating tank 6 to constitute an apex 6a formed at the upper part of the tank 6. The upper end of a discharge pipe 21 constituting a discharge means for removing the impurities outside the tank 6 by overflowing along with the bubbles liq. is opened in the closed part 6a. Meanwhile, the lower end of the discharge pipe 21 is opened outside the tank 6. Besides, the impurities such as the body fluid of fish mixed in the liq. are deposited on the bubble in the tank 6, the bubble is further grown, and the grown bubble is allowed to overflow the tank and automatically discharged outside the tank through the pipe 21.

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】この発明は、例えば活魚の水
槽に接続される圧力式循環ろ過装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pressure-type circulating filter connected to, for example, a live fish tank.

【0002】[0002]

【従来の技術】活魚の水槽は、食べ残しの餌や魚の体
液、糞等によって水が汚れるため、例えば圧力式循環ろ
過装置を備えるものがある。この圧力式循環ろ過装置に
は、特にろ過装置では処理が困難な魚の体液等の有機物
を除去するために、泡沫処理槽を備えることが知られて
いる。この泡沫処理槽では、液体に空気を吹き込み泡沫
状態にして液体に混入する魚の体液等の不純物を液面に
浮かせて除去している。
2. Description of the Related Art Some aquariums for live fish are provided with, for example, a pressure-type circulating filtration device because water is contaminated with food left uneaten, body fluid of fish, feces, and the like. It is known that this pressure-type circulating filtration device includes a foam treatment tank in order to remove organic substances such as body fluids of fish, which are particularly difficult to treat with the filtration device. In this foam treatment tank, air is blown into the liquid to form a foam, and impurities such as fish body fluid mixed into the liquid are removed by floating on the liquid surface.

【0003】[0003]

【発明が解決しようとする課題】上記泡沫処理槽におい
ては、液面に浮かぶ魚の体液等の不純物を除去する適切
な手段がなく、適当な時期に作業者が液面に泡に付着し
て浮かぶ魚の体液等の不純物を泡と共にすくって回収し
て外部に排出している。このように、手作業による除去
であり作業が面倒で、しかも非衛生的でもある。
In the above foam treatment tank, there is no proper means for removing impurities such as body fluids of fish floating on the surface of the liquid, and the worker adheres to the liquid surface and floats at the appropriate time. Impurities such as body fluids of fish are scooped and collected together with the foam and discharged to the outside. As described above, the removal is performed manually, which is troublesome and unsanitary.

【0004】この発明は、かかる点に鑑みてなされたも
ので、作業者の手作業によらないで、泡に付着して浮か
ぶ魚の体液等の不純物を泡と共に自動的に除去すること
ができる圧力式循環ろ過装置を提供することを目的とし
ている。
[0004] The present invention has been made in view of the above points, and a pressure capable of automatically removing impurities such as a body fluid of a fish which adheres to a foam and floats together with the foam without manual operation of an operator. It is an object of the present invention to provide a circulating filtration device.

【0005】[0005]

【課題を解決するための手段】前記課題を解決し、且つ
目的を達成するために、請求項1記載の発明は、液体を
泡沫状態にして液体に混入する不純物を除去する泡沫処
理槽を備える圧力式循環ろ過装置において、前記泡沫処
理槽の上部に密閉部を設け、さらに前記密閉部に前記不
純物を泡沫状態の液体と共に前記泡沫処理槽の外部に除
去する取出手段を設けたことを特徴としている。泡沫処
理槽で形成される泡に液体に混入する不純物が付着し、
泡がさらに成長していくと取出手段によって自動的に外
部に除去される。このように、作業者の手作業によらな
いで、泡に付着して浮かぶ魚の体液等の不純物を泡と共
に自動的に除去することができ、衛生的である。
In order to solve the above-mentioned problems and to achieve the object, the invention according to the first aspect of the present invention includes a foam treatment tank for converting a liquid into a foam to remove impurities mixed in the liquid. In the pressure-type circulating filtration device, a sealing portion is provided at an upper portion of the foam treatment tank, and a take-out means for removing the impurities to the outside of the foam treatment tank together with the liquid in a foam state is provided in the sealing portion. I have. The impurities mixed into the liquid adhere to the foam formed in the foam treatment tank,
As the bubbles grow further, they are automatically removed to the outside by the extraction means. In this manner, impurities such as body fluids of fish that adhere to and float on the foam can be automatically removed together with the foam without the manual operation of the worker, which is sanitary.

【0006】請求項2記載の発明の圧力式循環ろ過装置
は、前記密閉部の頂面を上方に凸形状の曲面に形成した
ことを特徴としている。泡沫処理槽の上部の密閉部の頂
面が上方に凸形状の曲面であるから、成長する泡が局部
的に溜まることなく移動して円滑に、泡に付着して浮か
ぶ魚の体液等の不純物を泡と共に自動的に除去すること
ができる。
The pressure-type circulating filtration apparatus according to the second aspect of the present invention is characterized in that the top surface of the closed portion is formed as a curved surface that is convex upward. Since the top surface of the closed part at the top of the foam treatment tank is a curved surface with an upward convex shape, the growing bubbles move smoothly without locally accumulating and smoothly remove impurities such as body fluids of fish that adhere to the bubbles and float. It can be removed automatically with the foam.

【0007】請求項3記載の発明の圧力式循環ろ過装置
は、前記密閉部の頂面の少なくとも一部を透明部材で形
成したことを特徴としている。泡沫処理槽の上部の密閉
部の頂面の少なくとも一部が透明部材で形成されている
から、外部から容易に泡に付着して浮かぶ魚の体液等の
不純物を泡と共に自動的に除去する状態を確認すること
ができ、さらに密閉部の汚れも容易に確認することがで
きる。
A pressure-type circulating filtration apparatus according to a third aspect of the present invention is characterized in that at least a part of a top surface of the closed portion is formed of a transparent member. Since at least a part of the top surface of the closed part at the top of the foam treatment tank is formed of a transparent member, a state in which impurities such as bodily fluids of fish that easily adhere to the foam from the outside and float together with the foam is automatically removed. It can be confirmed, and the contamination of the sealed portion can be easily confirmed.

【0008】請求項4記載の発明の圧力式循環ろ過装置
は、前記密閉部の頂面の少なくとも一部が着脱可能であ
ることを特徴としている。泡沫処理槽の上部の密閉部の
頂面の少なくとも一部が着脱可能であるから、魚の体液
等の不純物が集まり汚れ易い密閉部の頂面を外して洗浄
することができる。
[0008] A pressure-type circulating filtration apparatus according to a fourth aspect of the present invention is characterized in that at least a part of a top surface of the closed portion is detachable. Since at least a part of the top surface of the sealed portion at the top of the foam treatment tank is detachable, the top surface of the sealed portion where impurities such as body fluids of fish are easily collected and contaminated can be removed for cleaning.

【0009】請求項5記載の発明の圧力式循環ろ過装置
は、前記泡沫処理槽内の液体を上流側の液体タンクに戻
すサージタンクを備え、このサージタンクに前記泡沫処
理槽内の液体を導く戻しパイプを上下方向へ移動可能に
設けたことを特徴としている。泡沫処理槽内の液体を導
く戻しパイプを上下方向へ移動することで、泡沫処理槽
内の液面レベルを容易に調節することができ、除去する
魚の体液等の不純物の量を調整することができる。
The pressure-type circulating filtration apparatus according to the present invention has a surge tank for returning the liquid in the foam processing tank to an upstream liquid tank, and guides the liquid in the foam processing tank to the surge tank. The return pipe is provided so as to be movable in the vertical direction. By moving the return pipe that guides the liquid in the foam treatment tank up and down, the liquid level in the foam treatment tank can be easily adjusted, and the amount of impurities such as fish body fluid to be removed can be adjusted. it can.

【0010】請求項6記載の発明の圧力式循環ろ過装置
は、液体を洗浄する生物ろ過槽及び/または物理ろ過槽
と、前記請求項1乃至請求項5記載の泡沫処理槽と、前
記液体を加圧して前記生物ろ過槽及び/または物理ろ過
槽、密閉式泡沫処理槽に循環させる循環手段とを備える
ことを特徴としている。生物ろ過槽及び/または物理ろ
過槽と、請求項1乃至請求項5記載の泡沫処理槽に、液
体を加圧して循環させて液体に混入する不純物を除去し
て浄化することができる。
[0010] According to a sixth aspect of the present invention, there is provided a pressure-type circulating filtration apparatus, comprising: a biological filtration tank and / or a physical filtration tank for washing a liquid; a foam treatment tank according to the first to fifth aspects; It is characterized by comprising a circulating means for pressurizing and circulating through the biological filtration tank and / or the physical filtration tank and the closed type foam treatment tank. The liquid can be pressurized and circulated through the biological filtration tank and / or the physical filtration tank and the foam treatment tank according to the first to fifth aspects to remove impurities mixed in the liquid, thereby purifying the liquid.

【0011】請求項7記載の発明の圧力式循環ろ過装置
は、前記生物ろ過槽及び/または物理ろ過槽を密閉式と
し、この下流側に前記泡沫処理槽を配置し、さらに前記
生物ろ過槽及び/または物理ろ過槽、前記泡沫処理槽の
上流側に前記液体を加圧して送る液体圧送手段を配置し
たことを特徴としている。液体圧送手段を配置して液体
を圧送して泡沫処理槽、生物ろ過槽及び/または物理ろ
過槽へ容易に循環させることができ、効率的な液体の浄
化が可能である。
According to a seventh aspect of the present invention, there is provided a pressure-type circulating filtration apparatus wherein the biological filtration tank and / or the physical filtration tank are hermetically sealed, and the foam treatment tank is disposed downstream of the biological filtration tank and / or the physical filtration tank. And / or a liquid pressurizing means for pressurizing and sending the liquid is arranged upstream of the physical filtration tank and the foam treatment tank. The liquid pumping means is disposed, and the liquid can be pumped and easily circulated to the foam treatment tank, the biological filtration tank and / or the physical filtration tank, and the liquid can be efficiently purified.

【0012】請求項8記載の発明の圧力式循環ろ過装置
は、前記生物ろ過槽及び/または物理ろ過槽に、循環方
向とは逆方向へ液体を流して清掃する液体流路を設けた
ことを特徴としている。生物ろ過槽及び/または物理ろ
過槽に、循環方向とは逆方向へ液体を流す簡単な構造
で、かつ確実に生物ろ過槽及び/または物理ろ過槽を清
掃することができる。
The pressure-type circulating filtration apparatus according to the present invention is characterized in that the biological filtration tank and / or the physical filtration tank is provided with a liquid flow path for cleaning by flowing a liquid in a direction opposite to a circulation direction. Features. The biological filtration tank and / or the physical filtration tank can be reliably cleaned with a simple structure in which the liquid flows through the biological filtration tank and / or the physical filtration tank in a direction opposite to the circulation direction.

【0013】請求項9記載の発明の圧力式循環ろ過装置
は、生物ろ過槽及び/または物理ろ過槽の下流側に、泡
沫処理槽を配置し、液体を加圧して前記生物ろ過槽及び
/または物理ろ過槽、泡沫処理槽に循環させる循環手段
を備え、前記生物ろ過槽及び/または物理ろ過槽の上流
側と前記泡沫処理槽とを連通させるバイパス通路を設け
たことを特徴としている。液体をバイパス通路により泡
沫処理槽に導くことで総循環量を上げ酸素供給量を増加
することができる。また、生物ろ過槽及び/または物理
ろ過槽が仮に詰まることがあっても、液体をバイパス通
路により泡沫処理槽に導いて循環させて酸素を供給する
ことができる。
According to a ninth aspect of the present invention, there is provided a pressure-type circulating filtration apparatus, wherein a foam treatment tank is disposed downstream of a biological filtration tank and / or a physical filtration tank, and a liquid is pressurized to increase the pressure of the biological filtration tank and / or the biological filtration tank. It is characterized in that a circulation means for circulating through the physical filtration tank and the foam treatment tank is provided, and a bypass passage for communicating the upstream side of the biological filtration tank and / or the physical filtration tank with the foam treatment tank is provided. By guiding the liquid to the foam treatment tank through the bypass passage, the total circulation amount can be increased and the oxygen supply amount can be increased. Also, even if the biological filtration tank and / or the physical filtration tank may be clogged, oxygen can be supplied by circulating the liquid through the bypass passage to the foam treatment tank.

【0014】請求項10記載の発明の圧力式循環ろ過装
置は、前記泡沫処理槽の上部に液体入口を位置させると
ともに、下部に液体出口を位置させたことを特徴として
いる。液体が泡沫処理槽の上部の液体入口から入り、下
部の液体出口から取り出すことで流れが複雑になり酸素
の溶け込みを促すことができる。
The pressure-type circulating filtration apparatus according to the present invention is characterized in that a liquid inlet is located at an upper part of the foam treatment tank and a liquid outlet is located at a lower part. When the liquid enters the liquid inlet at the upper part of the foam treatment tank and is taken out from the liquid outlet at the lower part, the flow becomes complicated and the dissolution of oxygen can be promoted.

【0015】請求項11記載の発明の圧力式循環ろ過装
置は、前記生物ろ過槽及び/または物理ろ過槽の内部の
底部にエアストーンを配置し、このエアストーンに逆洗
浄前に空気を供給するエア通路に逆止弁を設けたことを
特徴としている。逆洗浄前にエア通路から空気を供給し
てエアレーションすることにより濾材の汚れを取り除き
洗浄効率を向上させる。
In the pressure-type circulating filtration apparatus according to the present invention, an airstone is disposed at the bottom inside the biological filtration tank and / or the physical filtration tank, and air is supplied to the airstone before back washing. A check valve is provided in the air passage. By supplying air from the air passage and performing aeration before the back washing, dirt on the filter medium is removed and the washing efficiency is improved.

【0016】請求項12記載の発明の圧力式循環ろ過装
置は、架台に前記泡沫処理槽及びろ過槽以外の装置構成
部品を配置し、この奥部に前記生物ろ過槽及び前記物理
ろ過槽を配置し、手前部に操作系を集中して配置し、さ
らに架台に配管系を取り付け、前記泡沫処理槽、前記装
置構成部品、前記生物ろ過槽及び前記物理ろ過槽をカバ
ーで覆ったことを特徴としている。架台に配管系を取り
付けることで、配管系が邪魔にならず架台に泡沫処理
槽、装置構成部品、生物ろ過槽及び物理ろ過槽をコンパ
クトに配置することができる。さらに、架台の手前部に
操作系を集中して配置することで、保守、点検が容易で
メンテナンス性が向上する。また、架台に配管系を取り
付けたから配管の配置が容易であり、しかも架台で配管
を隠すことができる。また、泡沫処理槽、装置構成部
品、生物ろ過槽及び物理ろ過槽がカバーで覆われてお
り、埃などから保護されると共に外観性が向上する。
According to a twelfth aspect of the present invention, there is provided a pressure-type circulating filtration apparatus in which equipment components other than the foam treatment tank and the filtration tank are arranged on a gantry, and the biological filtration tank and the physical filtration tank are arranged behind the apparatus. Then, the operation system is centrally arranged in the front part, a piping system is further attached to the gantry, and the foam treatment tank, the device components, the biological filtration tank and the physical filtration tank are covered with a cover. I have. By attaching the piping system to the gantry, the foam processing tank, the equipment components, the biological filtration tank, and the physical filtration tank can be compactly arranged on the gantry without disturbing the piping system. Furthermore, by arranging the operation system in the front of the gantry in a concentrated manner, maintenance and inspection are easy, and the maintainability is improved. Further, since the piping system is attached to the gantry, the arrangement of the piping is easy, and the tubing can hide the piping. Further, the foam treatment tank, the component parts of the apparatus, the biological filtration tank, and the physical filtration tank are covered with a cover, so that the appearance is improved while being protected from dust and the like.

【0017】請求項13記載の発明の圧力式循環ろ過装
置は、請求項8記載の前記液体流路は、前記生物ろ過槽
及び/または物理ろ過槽に液体を供給する第1通路と、
前記生物ろ過槽及び/または物理ろ過槽から液体を排出
する第2通路とで構成し、前記第1通路と第2通路を生
物ろ過槽及び/または物理ろ過槽の外部において互いに
集合させ、その集合部に液体の供給通路を接続する一
方、前記第1通路と第2通路にそれぞれ第1切換え弁と
第2切換え弁を前記生物ろ過槽及び/または物理ろ過槽
の外部において互いに隣接させて配置し、前記第1切換
え弁に液体を外部に排出するドレン配管を接続し、前記
第1切換え弁は、前記供給通路と第1通路とが連通した
状態と前記第1通賂とドレン配管とが連通した状態とを
切り換え可能に構成し、前記第2切換え弁は、前記供給
通路と第2通路とが連通した状態と非連通との状態とを
切り換え可能に構成したことを特徴としている。液体の
供給通路と第1通賂とが連通した状態と、液体を外部に
排出するドレン配管と第1通路とが連通した状態とを切
り換え可能に構成した第1切換え弁と、供給通路と第2
通路とが連通した状態と非連通との状態とを切り換え可
能に構成した第2切換え弁とを生物ろ過槽及び/または
物理ろ過槽の外部において互いに隣接させて配置したの
で、生物ろ過槽及び/または物理ろ過槽に循環方向とは
逆方向へ液体を流して清掃する作業を簡単に行うことが
できる。
According to a thirteenth aspect of the present invention, there is provided the pressure-type circulating filtration device according to the eighth aspect, wherein the liquid flow path according to the eighth aspect supplies a liquid to the biological filtration tank and / or the physical filtration tank,
A second passage for discharging liquid from the biological filtration tank and / or the physical filtration tank, wherein the first passage and the second passage are assembled together outside the biological filtration tank and / or the physical filtration tank, and A liquid supply passage is connected to the portion, and a first switching valve and a second switching valve are respectively arranged in the first passage and the second passage so as to be adjacent to each other outside the biological filtration tank and / or the physical filtration tank. A drain pipe for discharging a liquid to the outside is connected to the first switching valve, and the first switching valve is in a state where the supply passage and the first passage are in communication with each other and the first bribe and the drain pipe are in communication with each other. The second switching valve is configured to be switchable between a state in which the supply passage and the second passage communicate with each other and a state in which the supply passage and the second passage do not communicate with each other. A first switching valve configured to be able to switch between a state in which the liquid supply passage communicates with the first bribe and a state in which the drain pipe that discharges the liquid to the outside communicates with the first passage; 2
Since the second switching valve configured to be able to switch between a state of communication with the passage and a state of non-communication is arranged adjacent to each other outside the biological filtration tank and / or the physical filtration tank, the biological filtration tank and / or Alternatively, the cleaning operation can be easily performed by flowing the liquid in the direction opposite to the circulation direction in the physical filtration tank.

【0018】請求項14記載の発明の圧力式循環ろ過装
置は、請求項13記載の前記生物ろ過槽と物理ろ過槽を
互いに隣接して配置し、生物ろ過槽と物理ろ過槽にそれ
ぞれ前記第1切換え弁と第2切換え弁を設ける一方、こ
れら第1切換え弁と第2切換え弁を、前記生物ろ過槽お
よび物理ろ過槽に対して同じ側に配置することを特徴と
している。生物ろ過槽と物理ろ過槽にそれぞれ設けた第
1切換え弁と第2切換え弁を、生物ろ過槽及び物理ろ過
槽に対して同じ側に配置したので、生物ろ過槽と物理ろ
過槽の第1切換え弁及び第2切換え弁の切換え作業を容
易に行え、生物ろ過槽と物理ろ過槽を清掃する作業を簡
単に行うことができる。
According to a fourteenth aspect of the present invention, there is provided a pressure-type circulating filtration device, wherein the biological filtration tank and the physical filtration tank according to the thirteenth aspect are arranged adjacent to each other, and the first and second biological filtration tanks are respectively provided in the biological filtration tank and the physical filtration tank. A switching valve and a second switching valve are provided, and the first switching valve and the second switching valve are arranged on the same side with respect to the biological filtration tank and the physical filtration tank. Since the first switching valve and the second switching valve provided in the biological filtration tank and the physical filtration tank are arranged on the same side with respect to the biological filtration tank and the physical filtration tank, the first switching between the biological filtration tank and the physical filtration tank is performed. The switching operation of the valve and the second switching valve can be easily performed, and the operation of cleaning the biological filtration tank and the physical filtration tank can be easily performed.

【0019】[0019]

【発明の実施の形態】以下、圧力式循環ろ過装置の実施
例を図面に基づいて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a pressure-type circulating filtration apparatus will be described below with reference to the drawings.

【0020】まず、図1乃至図5の圧力式循環ろ過装置
の第1実施例について説明する。図1は圧力式循環ろ過
装置の第1実施例の平面図、図2は物理ろ過槽と泡沫処
理槽の概略構成図、図3は生物ろ過槽の概略構成図、図
4は泡沫処理槽のエジェクタの断面図、図5は泡沫処理
槽の上部の密閉部の他の実施例を示す図である。
First, a first embodiment of the pressure type circulating filtration apparatus shown in FIGS. 1 to 5 will be described. 1 is a plan view of a first embodiment of a pressure-type circulating filtration device, FIG. 2 is a schematic configuration diagram of a physical filtration tank and a foam treatment tank, FIG. 3 is a schematic configuration diagram of a biological filtration tank, and FIG. FIG. 5 is a cross-sectional view of the ejector, and FIG. 5 is a view showing another embodiment of the closed portion at the top of the foam processing tank.

【0021】圧力式循環ろ過装置1は、例えば活魚の水
槽2に接続され、液体である水槽2の水を循環して洗浄
するものである。圧力式循環ろ過装置1の架台3の上
に、物理ろ過槽4と、生物ろ過槽5と、泡沫処理槽6
と、活性炭槽7、紫外線殺菌槽8及び循環手段9が配置
され、架台3の上にコンパクトに配置されている。ま
た、活性炭槽7、紫外線殺菌槽8には、温度の調節を行
なう熱交換器10が接続されている。
The pressure-type circulating filtration device 1 is connected to, for example, a live fish tank 2 and circulates and cleans water in the water tank 2 as a liquid. A physical filtration tank 4, a biological filtration tank 5, and a foam treatment tank 6 are placed on a base 3 of the pressure-type circulating filtration device 1.
, An activated carbon tank 7, an ultraviolet sterilization tank 8, and a circulation means 9, and are compactly arranged on the gantry 3. A heat exchanger 10 for controlling the temperature is connected to the activated carbon tank 7 and the ultraviolet sterilization tank 8.

【0022】循環手段9は、水槽2からの水を圧送する
液体圧送手段である循環ポンプ11と、物理ろ過槽4、
生物ろ過槽5、泡沫処理槽6、活性炭槽7、紫外線殺菌
槽8、熱交換器10を循環させて水槽2へ戻す配管12
(12a〜12n)及び配管12に配置された切換弁1
3(13a〜13e)から構成される。生物ろ過槽5及
び物理ろ過槽4を密閉式とし、この物理ろ過槽4の下流
側に生物ろ過槽5が配置され、さらに生物ろ過槽5の下
流側に活性炭槽7、紫外線殺菌槽8、熱交換器10が配
置され、さらに下流側に密閉式の泡沫処理槽6が配置
し、物理ろ過槽4の上流側には循環ポンプ11が配置さ
れている。
The circulating means 9 includes a circulating pump 11 which is a liquid pumping means for pumping water from the water tank 2, and a physical filtration tank 4.
A pipe 12 for circulating the biological filtration tank 5, the foam treatment tank 6, the activated carbon tank 7, the ultraviolet sterilization tank 8, and the heat exchanger 10 to return to the water tank 2.
(12a to 12n) and switching valve 1 arranged in pipe 12
3 (13a to 13e). The biological filtration tank 5 and the physical filtration tank 4 are sealed, and the biological filtration tank 5 is disposed downstream of the physical filtration tank 4, and the activated carbon tank 7, the ultraviolet sterilization tank 8, and the heat An exchanger 10 is disposed, a hermetic foam treatment tank 6 is disposed further downstream, and a circulation pump 11 is disposed upstream of the physical filtration tank 4.

【0023】循環ポンプ11は、配管12a、切換弁1
3aを介して水槽2と接続され、循環時には切換弁13
aの操作で水槽2の水が配管12aを介して循環ポンプ
11へ送られるが、水槽2の洗浄時には切換弁13aの
操作で点線矢印で示すように洗浄水がドレン配管14を
介して回収される。循環ポンプ11と切換弁13aとの
間に、洗浄水を導く配管15が接続され、この配管15
に配置された切換弁16の操作で点線矢印で示す洗浄水
が配管12aへ供給される。
The circulation pump 11 includes a pipe 12a, a switching valve 1
3a is connected to the water tank 2 via the switching valve 13a.
By the operation of a, the water in the water tank 2 is sent to the circulation pump 11 through the pipe 12a. However, when the water tank 2 is washed, the washing water is recovered through the drain pipe 14 by the operation of the switching valve 13a as shown by a dotted arrow. You. A pipe 15 for leading washing water is connected between the circulation pump 11 and the switching valve 13a.
The washing water indicated by the dotted arrow is supplied to the pipe 12a by the operation of the switching valve 16 disposed in the pipe 12a.

【0024】物理ろ過槽4には、図2に示すように、上
部に密閉部4aが設けられ、物理ろ過槽4の内部には、
下方より大きい支持石層4b、小さい支持石層4c、無
煙炭層4dが上方向に積層され、循環ポンプ11からの
水が配管12b、切換弁13b、配管12cを介して上
方の密閉部4aから無煙炭層4dに供給される。水槽2
からの水は、無煙炭層4d、小さい支持石層4c、大き
い支持石層4bを流れることでろ過され、下側に接続さ
れた配管12d、切換弁13c、配管12e、切換弁1
3d、配管12fを介して生物ろ過槽5へ送られる。切
換弁13bには、ドレン配管17が接続されている。洗
浄時に切換弁13b,13cの操作で、循環ポンプ11
からの点線矢印の洗浄水を配管12b,12g,12
h、切換弁13cを介して物理ろ過槽4へ逆流させ、こ
の洗浄水が切換弁13bを介してドレン配管17から回
収される。
As shown in FIG. 2, the physical filtration tank 4 is provided with a sealing portion 4a at the upper part.
The supporting stone layer 4b, the supporting stone layer 4c, and the anthracite layer 4d, which are larger than the lower part, are stacked upward, and water from the circulation pump 11 flows from the upper sealed part 4a through the pipe 12b, the switching valve 13b, and the pipe 12c. It is supplied to the layer 4d. Aquarium 2
Is filtered by flowing through the anthracite layer 4d, the small support stone layer 4c, and the large support stone layer 4b, and the pipe 12d, the switching valve 13c, the pipe 12e, and the switching valve 1 connected to the lower side are filtered.
3d, sent to the biological filtration tank 5 via the pipe 12f. A drain pipe 17 is connected to the switching valve 13b. At the time of washing, the circulation pump 11 is operated by operating the switching valves 13b and 13c.
From the pipes 12b, 12g, 12
h, the water is returned to the physical filtration tank 4 via the switching valve 13c, and the washing water is recovered from the drain pipe 17 via the switching valve 13b.

【0025】生物ろ過槽5には、図3に示すように、上
部に密閉部5aが設けられ、生物ろ過槽5の内部には、
サンゴ層5bが積層され、物理ろ過槽4からの水が配管
12fを介して下方からサンゴ層5bに供給される。サ
ンゴ層5bでろ過された水槽2の水は、密閉部5aから
配管12iを介して下方から取り出され、下側に接続さ
れた配管12j、切換弁13e、配管12kを介して活
性炭槽7、紫外線殺菌槽8へ供給される。活性炭槽7で
色素を取り、紫外線殺菌槽8で殺菌される。切換弁13
dには、ドレン配管18が接続されている。洗浄時に
は、切換弁13e,13dの操作で、循環ポンプ11か
らの点線矢印の洗浄水を配管12b,12g,12l、
切換弁13eを介して生物ろ過槽5へ逆流させ、この洗
浄水が切換弁13dを介してドレン配管18から回収さ
れる。
As shown in FIG. 3, the biological filtration tank 5 is provided with a sealing portion 5a at the upper part.
The coral layer 5b is laminated, and water from the physical filtration tank 4 is supplied to the coral layer 5b from below through the pipe 12f. The water in the water tank 2 filtered by the coral layer 5b is taken out from below through the closed part 5a via the pipe 12i, and is activated via the pipe 12j, the switching valve 13e, and the pipe 12k connected to the lower side, and It is supplied to the sterilization tank 8. The pigment is removed in the activated carbon tank 7 and sterilized in the ultraviolet sterilization tank 8. Switching valve 13
A drain pipe 18 is connected to d. At the time of washing, the operation of the switching valves 13e and 13d allows the washing water indicated by the dotted arrow from the circulation pump 11 to be supplied to the pipes 12b, 12g,
The water is returned to the biological filtration tank 5 via the switching valve 13e, and the washing water is recovered from the drain pipe 18 via the switching valve 13d.

【0026】泡沫処理槽6は、液体を泡沫状態にして液
体に混入する不純物を除去するものであり、図2に示す
ように、熱交換器10から配管12nを介して水槽2の
水が上部から供給される。この泡沫処理槽6の上部に
は、密閉部6aが設けられている。物理ろ過槽4の出口
に接続した配管12eを2つに分岐し、一方の配管12
mを泡沫処理槽6の下部に接続し、この分岐した配管1
2mにエジェクタ19を設けている。このエジェクタ1
9には、図4に示すように大気開放したパイプ20の一
端をオリフィス19aに開口している。オリフィス19
aで水の流速が増し、そこでパイプ20から空気を吸い
込み泡沫処理槽6の下部に空気を供給し、泡を発生させ
るエア源としている。泡沫処理槽6に空気を送るための
エアポンプを必要とせず、構成が簡単である。
The foam treatment tank 6 removes impurities mixed in the liquid by making the liquid into a foam state. As shown in FIG. 2, water in the water tank 2 is supplied from the heat exchanger 10 through a pipe 12n. Supplied from Above the foam processing tank 6, a closed portion 6a is provided. The pipe 12e connected to the outlet of the physical filtration tank 4 is branched into two,
m is connected to the lower part of the foam treatment tank 6, and the branched pipe 1
An ejector 19 is provided at 2 m. This ejector 1
In FIG. 9, one end of a pipe 20 opened to the atmosphere is opened to an orifice 19a as shown in FIG. Orifice 19
The flow velocity of the water increases at a, and the air is sucked in from the pipe 20 and supplied to the lower part of the foam processing tank 6 to serve as an air source for generating bubbles. An air pump for sending air to the foam processing tank 6 is not required, and the configuration is simple.

【0027】泡沫処理槽6の上部には、透明なプラスチ
ックからなると共に上方に凸形状の蓋体6bが着脱自在
に取り付けられている。この蓋体6bが、泡沫処理槽6
の上部に形成された密閉部6aの頂面を形成している。
密閉部6aには、不純物を泡沫状態の液体と共にオーバ
ーフローにより泡沫処理槽6の外部に除去する取出手段
を構成する取出パイプ21の上端が開口している。な
お、この取出パイプ21の下端は泡沫処理槽6の外部に
開口している。泡沫処理槽6で形成される泡に液体に混
入する魚の体液等の不純物が付着し、泡がさらに成長し
ていくとオーバーフローして自動的に取出パイプ21を
介して外部に除去される。このように、作業者の手作業
によらないで、泡に付着して浮かぶ魚の体液等の不純物
を泡と共に自動的に除去することができ、しかも衛生的
である。
A lid 6b made of transparent plastic and having an upward convex shape is detachably attached to the upper part of the foam processing tank 6. This lid 6b is used for the foam treatment tank 6
Of the sealing portion 6a formed on the upper portion of the upper portion.
The sealing section 6a has an opening at the upper end of an extraction pipe 21 that constitutes extraction means for removing impurities to the outside of the foam treatment tank 6 by overflowing together with the liquid in the foam state. Note that the lower end of the take-out pipe 21 is open to the outside of the foam treatment tank 6. Impurities such as fish body fluid mixed into the liquid adhere to the foam formed in the foam processing tank 6. When the foam further grows, it overflows and is automatically removed to the outside via the extraction pipe 21. In this manner, impurities such as body fluids of fish that adhere to and float on the foam can be automatically removed together with the foam without the manual operation of the worker, which is sanitary.

【0028】泡沫処理槽6の上部の密閉部6aの頂面を
形成する蓋体6bは、上方に凸形状の曲面に形成され、
密閉部6aの頂面が曲面であるから、成長する泡が局部
的に溜まることなく移動して円滑に取出パイプ21から
オーバーフローすることができる。
The lid 6b, which forms the top surface of the sealing portion 6a at the top of the foam treatment tank 6, is formed to have an upwardly convex curved surface.
Since the top surface of the sealing portion 6a is a curved surface, the growing bubbles can move without locally accumulating and overflow from the extraction pipe 21 smoothly.

【0029】また、蓋体6bが透明部材で形成されてい
るため、外部から容易に泡に付着して浮かぶ魚の体液等
の不純物を泡と共に自動的に除去する状態を確認するこ
とができ、さらに密閉部6aの汚れも容易に確認するこ
とができる。
Further, since the lid 6b is formed of a transparent member, it is possible to confirm a state in which impurities such as the body fluid of the fish which easily adhere to the bubbles from the outside and are automatically removed together with the bubbles, and furthermore, Dirt on the sealing portion 6a can also be easily confirmed.

【0030】さらに、蓋体6bは、ボルト22で泡沫処
理槽6の上部に締付固定されて密閉部6aの頂面が着脱
可能である。このように、泡沫処理槽6の上部の密閉部
6aの頂面が着脱可能であるから、魚の体液等の不純物
が集まり汚れ易い密閉部6aの頂面を外して洗浄するこ
とができる。
Further, the lid 6b is fastened and fixed to the upper part of the foam treatment tank 6 with bolts 22, and the top surface of the sealing portion 6a is detachable. As described above, since the top surface of the sealing portion 6a at the upper portion of the foam treatment tank 6 is detachable, the top surface of the sealing portion 6a where impurities such as body fluids of fish are easily collected and contaminated can be removed for cleaning.

【0031】また、蓋体6bは、図5に示すように、ワ
ンタッチで着脱可能にするようにしてもよい。即ち、泡
沫処理槽6の上部に一対の支持体23を設け、この支持
体23には係合切欠23aが設けられている。一方、密
閉部6aの中央上部に、取付バー24に設けた押圧体2
5を当てがい、取付バー24を回転して一対の支持体2
3の係合切欠23aに係合させると、取付バー24の押
圧体25により蓋体6bが下方に押されて泡沫処理槽6
の上部に密着される。
As shown in FIG. 5, the lid 6b may be made detachable with one touch. That is, a pair of supports 23 is provided above the foam processing tank 6, and the supports 23 are provided with engagement notches 23a. On the other hand, the pressing body 2 provided on the mounting bar 24 is provided above the center of the sealing portion 6a.
5 and rotate the mounting bar 24 to rotate the pair of support members 2.
3, the lid 6b is pushed downward by the pressing body 25 of the mounting bar 24, and the foam processing tank 6
Adhered to the top of

【0032】泡沫処理槽6の側部には、泡沫処理槽6内
の液体を上流側の液体タンクである水槽2に戻すサージ
タンク26が備えられている。このサージタンク26に
は、泡沫処理槽6内の水を導く戻しパイプ27の上端開
口が臨んでおり、この戻しパイプ27の上端部には、上
下方向へ移動可能なスライド管27aが接続され、この
スライド管27aを上下方向へ移動することで、泡沫処
理槽6内の液面レベルを容易に調節することができ、オ
ーバーフローにより除去する魚の体液等の不純物の量を
調整することができる。すなわち、泡沫処理槽6の液面
とサージタンク26の液面とは、ほぼ同一高さになるか
ら、例えば除去する不純物の量が多い時はスライド管2
7aを下げて泡沫処理槽6の液面を下げればよい。
On the side of the foam treatment tank 6, a surge tank 26 for returning the liquid in the foam treatment tank 6 to the water tank 2, which is the liquid tank on the upstream side, is provided. An upper end opening of a return pipe 27 that guides water in the foam treatment tank 6 faces the surge tank 26, and a slide pipe 27 a that can move in a vertical direction is connected to an upper end of the return pipe 27. By moving the slide tube 27a in the vertical direction, the liquid level in the foam treatment tank 6 can be easily adjusted, and the amount of impurities such as body fluids of fish to be removed by overflow can be adjusted. That is, since the liquid level of the foam treatment tank 6 and the liquid level of the surge tank 26 are substantially the same, for example, when the amount of impurities to be removed is large, the slide tube 2
7a may be lowered to lower the liquid level of the foam treatment tank 6.

【0033】圧力式循環ろ過装置1は、循環時に、切換
弁13a,13b,13c,13dの操作で、水槽2の
水を実線矢印で示す方向へ圧送して物理ろ過槽4、生物
ろ過槽5、紫外線殺菌槽8、活性炭槽7、熱交換器10
及び泡沫処理槽6を介して水槽2へ容易に循環させるこ
とができ、効率的な液体の浄化が可能である。
During circulation, the pressure-type circulating filtration device 1 sends the water in the water tank 2 in the direction indicated by the solid line arrow by operating the switching valves 13a, 13b, 13c, 13d to perform physical filtration and biological filtration. , Ultraviolet sterilization tank 8, activated carbon tank 7, heat exchanger 10
In addition, the liquid can be easily circulated to the water tank 2 via the foam processing tank 6, and the liquid can be efficiently purified.

【0034】また、圧力式循環ろ過装置1には、物理ろ
過槽4、生物ろ過槽5へ循環方向とは逆方向へ液体を流
して清掃する液体流路を設けられており、洗浄時に、切
換弁16,13b,13c,13d,13eの切り換え
操作で、配管15から洗浄水を点線矢印で示す方向へ圧
送して物理ろ過槽4、生物ろ過槽5へ循環方向とは逆方
向へ洗浄水を流して清掃し、簡単な構造で、かつ確実に
生物ろ過槽5及び物理ろ過槽4を清掃することができ
る。
The pressure-type circulating filtration apparatus 1 is provided with a liquid flow path for cleaning by flowing a liquid in a direction opposite to the circulation direction to the physical filtration tank 4 and the biological filtration tank 5. By switching the valves 16, 13 b, 13 c, 13 d, and 13 e, the washing water is pressure-fed from the pipe 15 in the direction indicated by the dotted line arrow, and the washing water is supplied to the physical filtration tank 4 and the biological filtration tank 5 in a direction opposite to the circulation direction. It is possible to clean the biological filtration tank 5 and the physical filtration tank 4 with a simple structure and surely by cleaning by flowing.

【0035】次に、図6及び図7の圧力式循環ろ過装置
の第2実施例について説明する。図6は圧力式循環ろ過
装置の第2実施例の平面図、図7は泡沫処理槽の概略構
成図である。
Next, a description will be given of a second embodiment of the pressure-type circulating filtration apparatus shown in FIGS. FIG. 6 is a plan view of a second embodiment of the pressure-type circulating filtration apparatus, and FIG. 7 is a schematic configuration diagram of a foam treatment tank.

【0036】この第2実施例の圧力式循環ろ過装置1
は、図1乃至図5と同じに構成されるものは、同じ符号
を付して説明を省略する。この第2実施例の圧力式循環
ろ過装置1は、泡沫処理槽6の下部にエアストーン30
が配置され、エアポンプ31から空気がパイプ32を介
してエアストーン30に供給され、エアストーン30に
よって泡沫が形成される。
The pressure type circulating filtration apparatus 1 of the second embodiment
The same components as those in FIGS. 1 to 5 are denoted by the same reference numerals and description thereof is omitted. The pressure type circulating filtration device 1 of the second embodiment includes an air stone 30
Is arranged, and air is supplied from the air pump 31 to the air stone 30 via the pipe 32, and foam is formed by the air stone 30.

【0037】次に、図8及び図9の圧力式循環ろ過装置
の第3実施例について説明する。図8は圧力式循環ろ過
装置の第3実施例の平面図、図9はサイクロン装置とエ
ジェクタトの概略構成図である。
Next, a description will be given of a third embodiment of the pressure-type circulating filtration apparatus shown in FIGS. FIG. 8 is a plan view of a third embodiment of a pressure-type circulating filtration device, and FIG. 9 is a schematic configuration diagram of a cyclone device and an ejecta.

【0038】この第3実施例の圧力式循環ろ過装置1
は、図1乃至図5と同じに構成されるものは、同じ符号
を付して説明を省略する。この第3実施例の圧力式循環
ろ過装置1は、物理ろ過槽4の代わりにサイクロン装置
40とエジェクタト50とを設けている。サイクロン装
置40の貯留部40aに不純物が堆積され、堆積された
ドレンは排出バルブ41の操作により排出される。サイ
クロン装置40のサイクロン部40bには、エジェクタ
ト50で空気パイプ51から吸入される空気と配管12
aからの水とを混合して供給され、サイクロン部40b
で不純物が分離されて下方の貯留部40aに堆積され
る。貯留部40aには、図9(b)に示すような舞い上
がり防止板42がブラケット42aを介して取り付けら
れている。サイクロン部40bに溜まる水は、循環ポン
プ11の駆動で配管12xを介して吸引され、循環ポン
プ11から生物ろ過槽5へ供給される。このサイクロン
装置40は濾材を必要としないため、濾材の目詰まりが
なく、常に安定したろ過を行なうことができる。
The pressure type circulating filtration device 1 of the third embodiment
The same components as those in FIGS. 1 to 5 are denoted by the same reference numerals and description thereof is omitted. The pressure type circulating filtration device 1 of the third embodiment is provided with a cyclone device 40 and an ejectat 50 instead of the physical filtration tank 4. Impurities are deposited in the storage section 40 a of the cyclone device 40, and the deposited drain is discharged by operating the discharge valve 41. The air sucked from the air pipe 51 by the ejector 50 and the pipe 12 are provided in the cyclone portion 40 b of the cyclone device 40.
a from the water from the cyclone 40b
Then, the impurities are separated and deposited in the lower storage section 40a. A rising prevention plate 42 as shown in FIG. 9B is attached to the storage section 40a via a bracket 42a. The water accumulated in the cyclone unit 40b is sucked through the pipe 12x by the driving of the circulation pump 11, and is supplied from the circulation pump 11 to the biological filtration tank 5. Since the cyclone device 40 does not require a filter medium, there is no clogging of the filter medium, and stable filtration can always be performed.

【0039】次に、図10乃至図12の圧力式循環ろ過
装置の第4実施例について説明する。図10は圧力式循
環ろ過装置の第4実施例の平面図、図11は物理ろ過槽
を洗浄する状態を示す図、図12は生物ろ過槽を洗浄す
る状態を示す図である。
Next, a fourth embodiment of the pressure-type circulating filtration apparatus shown in FIGS. 10 to 12 will be described. FIG. 10 is a plan view of a fourth embodiment of a pressure-type circulating filtration apparatus, FIG. 11 is a view showing a state of cleaning a physical filtration tank, and FIG. 12 is a view showing a state of cleaning a biological filtration tank.

【0040】この第4実施例の圧力式循環ろ過装置1
は、図6及び図7の第2実施例の圧力式循環ろ過装置と
同じに構成されるが、構成部品の配置が異なっている。
The pressure type circulating filtration device 1 of the fourth embodiment
Is configured the same as the pressure-type circulating filtration apparatus of the second embodiment shown in FIGS. 6 and 7, but the arrangement of the components is different.

【0041】この実施の形態では、物理ろ過槽4と生物
ろ過槽5を互いに隣接して配置し、液体流路は、生物ろ
過槽5及び物理ろ過槽4に液体を供給する第1通路7
5,77と、物理ろ過槽4及び生物ろ過槽5から液体を
排出する第2通路76,78とで構成している。第1通
路75,77と第2通路76,78を物理ろ過槽4及び
生物ろ過槽5の外部において互いに集合させ、その集合
部79,80に液体の供給通路81,82を接続する一
方、第1通路75,77と第2通路76,78にそれぞ
れ第1切換え弁70,73と第2切換え弁71,74を
物理ろ過槽4及び生物ろ過槽5の外部において互いに隣
接させて配置している。第1切換え弁70,73に液体
を外部に排出するドレン配管72を接続し、第1切換え
弁70,73は、供給通路81,82と第1通路75,
77とが連通した状態と第1通賂75,77とドレン配
管72とが連通した状態とを切り換え可能に構成してい
る。第2切換え弁71,74は、供給通路81,82と
第2通路76,78とが連通した状態と非連通との状態
とを切り換え可能に構成している。
In this embodiment, the physical filtration tank 4 and the biological filtration tank 5 are arranged adjacent to each other, and the liquid flow path is a first passage 7 for supplying a liquid to the biological filtration tank 5 and the physical filtration tank 4.
5, 77, and second passages 76, 78 for discharging liquid from the physical filtration tank 4 and the biological filtration tank 5. The first passages 75 and 77 and the second passages 76 and 78 are gathered together outside the physical filtration tank 4 and the biological filtration tank 5, and the liquid supply passages 81 and 82 are connected to the gathering portions 79 and 80, respectively. The first switching valves 70 and 73 and the second switching valves 71 and 74 are disposed adjacent to each other outside the physical filtration tank 4 and the biological filtration tank 5 in the first passages 75 and 77 and the second passages 76 and 78, respectively. . A drain pipe 72 for discharging liquid to the outside is connected to the first switching valves 70 and 73, and the first switching valves 70 and 73 are connected to the supply passages 81 and 82 and the first passages 75 and 75, respectively.
77 and a state in which the first bribes 75 and 77 and the drain pipe 72 are in communication with each other. The second switching valves 71 and 74 are configured to be able to switch between a state in which the supply passages 81 and 82 and the second passages 76 and 78 are in communication and a state in which they are not in communication.

【0042】循環時には、図10に示すように水槽2か
らの水が、循環ポンプ11、液体の供給通路81、第1
切換え弁70、第1通路75、物理ろ過槽4、第2通路
76、第2切換え弁71、液体の供給通路82、第1切
換え弁73、第1通賂77、生物ろ過槽5、第2通路7
8、第2切換え弁74、熱交換器10、活性炭槽7、紫
外線殺菌槽8、流量調整オリフィス60、泡沫処理槽
6、サージタンク26から水槽2に戻り、物理ろ過槽4
及び生物ろ過槽5からのドレンは、ドレン配管61から
回収される。
At the time of circulation, as shown in FIG. 10, water from the water tank 2 is supplied to the circulation pump 11, the liquid supply passage 81, the first
Switching valve 70, first passage 75, physical filtration tank 4, second passage 76, second switching valve 71, liquid supply passage 82, first switching valve 73, first bribe 77, biological filtration tank 5, second Passage 7
8, the second switching valve 74, the heat exchanger 10, the activated carbon tank 7, the ultraviolet sterilizing tank 8, the flow rate adjusting orifice 60, the foam treatment tank 6, and the surge tank 26 return to the water tank 2, and the physical filtration tank 4
The drain from the biological filtration tank 5 is collected from a drain pipe 61.

【0043】物理ろ過槽4の洗浄は、図11に示すよう
に、第1切換え弁70を、供給通路81と第1通路75
との連通を阻止するとともに第1通路75とドレン配管
72とを連通する状態に切り換え、第2切換え弁71
を、供給通路81と第2通路76とを連通する状態に切
り換える。この第1切換え弁70及び第2切換え弁71
の操作で、循環ポンプ11からの洗浄水が供給通路8
1、第2切換え弁71、第2通路76、物理ろ過槽4、
第1通路75、第1切換え弁70の順に循環方向と逆方
向に流れて物理ろ過槽4を清掃してドレン配管72から
回収される。
As shown in FIG. 11, when cleaning the physical filtration tank 4, the first switching valve 70 is connected to the supply passage 81 and the first passage 75.
Communication between the first passage 75 and the drain pipe 72 and the second switching valve 71
Is switched to a state in which the supply passage 81 and the second passage 76 are communicated with each other. The first switching valve 70 and the second switching valve 71
By the operation described above, the washing water from the circulation pump 11 is supplied to the supply passage 8.
1, second switching valve 71, second passage 76, physical filtration tank 4,
It flows in the order opposite to the circulation direction in the order of the first passage 75 and the first switching valve 70, cleans the physical filtration tank 4, and is collected from the drain pipe 72.

【0044】生物ろ過槽5の洗浄は、図12に示すよう
に、第1切換え弁73を、供給通路82と第1通路77
との連通を阻止するとともに第1通路77とドレン配管
72とを連通する状態に切り換え、第2切換え弁74
を、供給通路82と第2通路78とを連通する状態に切
り換える。この第1切換弁73及び第2切換え弁74の
操作で、循環ポンプ11からの洗浄水が供給通路81、
第1切換え弁70、第1通路75、物理ろ過槽4、第2
通路76、第2切換え弁71、供給通路82、第2切換
え弁74、第2通路78、生物ろ過槽5、第1通路7
7、第1切換弁73の順であり、生物ろ過槽5では循環
方向と逆方向に流れて生物ろ過槽5を清掃してドレン配
管72から回収される。
As shown in FIG. 12, when cleaning the biological filtration tank 5, the first switching valve 73 is connected to the supply passage 82 and the first passage 77.
Communication between the first passage 77 and the drain pipe 72 and the second switching valve 74
Is switched to a state in which the supply passage 82 and the second passage 78 communicate with each other. By operating the first switching valve 73 and the second switching valve 74, the washing water from the circulation pump 11 is supplied to the supply passage 81,
First switching valve 70, first passage 75, physical filtration tank 4, second
Passage 76, second switching valve 71, supply passage 82, second switching valve 74, second passage 78, biological filtration tank 5, first passage 7
7. In the order of the first switching valve 73, the biological filtration tank 5 flows in the direction opposite to the circulation direction, cleans the biological filtration tank 5, and is collected from the drain pipe 72.

【0045】このように、液体の供給通路81,82と
第1通賂75,77とが連通した状態と、液体を外部に
排出するドレン配管72と第1通路75,77とが連通
した状態とを切り換え可能に構成した第1切換え弁7
0,73と、供給通路81,82と第2通路76,78
とが連通した状態と非連通との状態とを切り換え可能に
構成した第2切換え弁71,74とを物理ろ過槽4及び
生物ろ過槽5の外部において互いに隣接させて配置した
ので、物理ろ過槽4及び生物ろ過槽5に循環方向とは逆
方向へ液体を流して清掃する作業を簡単に行うことがで
きる。
As described above, the state in which the liquid supply passages 81 and 82 communicate with the first bribes 75 and 77 and the state in which the drain pipe 72 for discharging the liquid to the outside communicates with the first passages 75 and 77. Switching valve 7 configured to be able to switch between
0, 73, supply passages 81, 82 and second passages 76, 78
Since the second switching valves 71 and 74 configured to be able to switch between a state in which they communicate with each other and a state in which they do not communicate are arranged adjacent to each other outside the physical filtration tank 4 and the biological filtration tank 5, the physical filtration tank The cleaning operation can be easily performed by flowing the liquid in the direction opposite to the circulation direction to the biological filtration tank 4 and the biological filtration tank 5.

【0046】また、物理ろ過槽4と生物ろ過槽5を互い
に隣接して配置し、物理ろ過槽4と生物ろ過槽5にそれ
ぞれ第1切換え弁70,73と第2切換え弁71,74
を設ける一方、これら第1切換え弁70,73と第2切
換え弁71,74を、物理ろ過槽4及び生物ろ過槽5に
対して同じ側に配置している。即ち、図10乃至図12
の実施の形態では、第1切換え弁70,73と第2切換
え弁71,74を、物理ろ過槽4及び生物ろ過槽5に対
して図中下側に配置している。
The physical filtration tank 4 and the biological filtration tank 5 are disposed adjacent to each other, and the physical filtration tank 4 and the biological filtration tank 5 are respectively provided with first switching valves 70 and 73 and second switching valves 71 and 74.
The first switching valves 70 and 73 and the second switching valves 71 and 74 are arranged on the same side with respect to the physical filtration tank 4 and the biological filtration tank 5. That is, FIGS. 10 to 12
In the embodiment, the first switching valves 70 and 73 and the second switching valves 71 and 74 are arranged below the physical filtration tank 4 and the biological filtration tank 5 in the figure.

【0047】このように、物理ろ過槽4と生物ろ過槽5
にそれぞれ設けた第1切換え弁70,73と第2切換え
弁71,74を、物理ろ過槽4及び生物ろ過槽5に対し
て同じ側に配置したので、物理ろ過槽4と生物ろ過槽5
の第1切換え弁70,73及び第2切換え弁71,74
の切換え作業を容易に行え、物理ろ過槽4と生物ろ過槽
5を清掃する作業を簡単に行うことができる。
As described above, the physical filtration tank 4 and the biological filtration tank 5
Since the first switching valves 70 and 73 and the second switching valves 71 and 74 provided on the same side with respect to the physical filtration tank 4 and the biological filtration tank 5, respectively, the physical filtration tank 4 and the biological filtration tank 5 are provided.
First switching valves 70, 73 and second switching valves 71, 74
Can be easily performed, and the operation of cleaning the physical filtration tank 4 and the biological filtration tank 5 can be easily performed.

【0048】なお、前記各実施例は、活魚の水槽の水の
浄化について説明したが、これに限定される液体の浄化
に広く適用できる。
In each of the embodiments described above, the purification of the water in the aquarium for live fish has been described. However, the present invention can be widely applied to the purification of liquid limited to this.

【0049】次に、図13乃至図21の圧力式循環ろ過
装置の第5実施例について説明する。図13は圧力式循
環ろ過装置の正面図、図14は圧力式循環ろ過装置の平
面図、図15は圧力式循環ろ過装置の右側面図、図16
は圧力式循環ろ過装置の左側面図、図17は一部のカバ
ーを外した状態の正面図、図18は一部のカバーを外し
た状態の平面図、図19は一部のカバーを外した状態の
右側面図、図20は一部のカバーを外した状態の左側面
図、図21は圧力式循環ろ過装置の分解斜視図である。
Next, a description will be given of a fifth embodiment of the pressure-type circulating filtration apparatus shown in FIGS. FIG. 13 is a front view of the pressure-type circulation filtration device, FIG. 14 is a plan view of the pressure-type circulation filtration device, FIG. 15 is a right side view of the pressure-type circulation filtration device, and FIG.
Is a left side view of the pressure-type circulating filtration device, FIG. 17 is a front view in a state where a part of the cover is removed, FIG. 18 is a plan view in a state where a part of the cover is removed, and FIG. FIG. 20 is a left side view with a part of the cover removed, and FIG. 21 is an exploded perspective view of the pressure-type circulating filtration device.

【0050】この第5実施例の圧力式循環ろ過装置1
は、図1乃至図5と同じに構成されるものは、同じ符号
を付して説明を省略する。圧力式循環ろ過装置1の架台
3は、高い中央部3aと、低い奥部3bと手前部3cと
を有しており、高い中央部3a上に、泡沫処理槽6及び
ろ過槽以外の装置構成部品100を配置し、この低い奥
部3bに生物ろ過槽5及び物理ろ過槽4を配置し、低い
手前部3cに操作系110を集中して配置している。
The pressure type circulating filtration device 1 of the fifth embodiment
The same components as those in FIGS. 1 to 5 are denoted by the same reference numerals and description thereof is omitted. The gantry 3 of the pressure-type circulating filtration device 1 has a high central portion 3a, a low inner portion 3b, and a front portion 3c. On the high central portion 3a, a device configuration other than the foam treatment tank 6 and the filtration tank is provided. The parts 100 are arranged, the biological filtration tank 5 and the physical filtration tank 4 are arranged in the lower inner part 3b, and the operation system 110 is concentrated in the lower front part 3c.

【0051】ろ過槽以外の装置構成部品100は、熱交
換器101、エアポンプ104、エア分岐管105、循
環ポンプ11、活性炭槽7、紫外線殺菌槽8及び熱交換
器10等から構成されている。熱交換器101は熱交換
タンク101a、コンディショニングユニット101
b、エアコンプレッサ101cから構成される。泡沫処
理槽6はカバー150、装置構成部品100はカバー1
51、生物ろ過槽5はカバー152及び物理ろ過槽4は
カバー153で覆われており、埃などから保護されると
共に外観性が向上する。カバー151にはコントローラ
154が取り付けられている。
The apparatus components 100 other than the filtration tank are composed of a heat exchanger 101, an air pump 104, an air branch pipe 105, a circulation pump 11, an activated carbon tank 7, an ultraviolet sterilization tank 8, a heat exchanger 10, and the like. The heat exchanger 101 includes a heat exchange tank 101a and a conditioning unit 101.
b, composed of an air compressor 101c. The foam treatment tank 6 has a cover 150, and the apparatus component 100 has a cover 1
51, the biological filtration tank 5 is covered with a cover 152 and the physical filtration tank 4 is covered with a cover 153, and is protected from dust and the like, and the appearance is improved. The controller 154 is attached to the cover 151.

【0052】架台3には、配管系160が取り付けら
れ、さらに配管系160には操作系170が配置されて
いる。配管系160は水槽2からの水を圧送する循環ポ
ンプ11と、物理ろ過槽4、生物ろ過槽5、泡沫処理槽
6、活性炭槽7、紫外線殺菌槽8を循環させて水槽2へ
戻す配管200(200a〜200l)で構成されてい
る。配管200b,200c,200d,200f,2
00g,200hは、架台3の高い中央部3aに前後方
向に貫通して取り付けられ、架台3で配管を隠すことが
でき、外観性が向上する。循環ポンプ11には、遠心ポ
ンプを用いている。
The gantry 3 is provided with a piping system 160, and the piping system 160 is further provided with an operation system 170. A piping system 160 circulates the circulation pump 11 for pumping water from the water tank 2, the physical filtration tank 4, the biological filtration tank 5, the foam treatment tank 6, the activated carbon tank 7, and the ultraviolet sterilization tank 8 and returns the pipe 200 to the water tank 2. (200a to 200l). Piping 200b, 200c, 200d, 200f, 2
00g and 200h are attached to the high center part 3a of the gantry 3 so as to penetrate in the front-rear direction, and the gantry 3 can hide the piping, thereby improving the appearance. As the circulation pump 11, a centrifugal pump is used.

【0053】操作系170は液体の循環方向をろ過方向
と洗浄方向へ切り換える切換弁300(300a〜30
0d)から構成され、架台3の低い手前部3cを集中し
て配置することで、前側から容易に切り換え操作するこ
とができるとともに、保守、点検が容易でメンテナンス
性が向上する。
The operation system 170 is provided with a switching valve 300 (300a-30) for switching the liquid circulation direction between the filtration direction and the washing direction.
0d), and by arranging the lower front portion 3c of the gantry 3 in a concentrated manner, the switching operation can be easily performed from the front side, and maintenance and inspection are easy and the maintainability is improved.

【0054】架台3に配管系160を取り付けること
で、配管系160が邪魔にならず架台3に泡沫処理槽
6、装置構成部品100、生物ろ過槽5及び物理ろ過槽
4がコンパクトに配置され、かつ配置の自由度が向上す
る。また、装置構成部品100の比較的保守、点検が必
要な活性炭槽7、紫外線殺菌槽8を熱交換器101の上
方に配置され、しかも生物ろ過槽5及び物理ろ過槽4よ
り手前側に位置しているからメンテナンスが容易であ
る。また、架台3に配管系160を取り付けたから配管
200(200a〜200l)の配置が容易である。
By attaching the piping system 160 to the gantry 3, the piping system 160 is not obstructed, and the foam treatment tank 6, the equipment component 100, the biological filtration tank 5, and the physical filtration tank 4 are compactly arranged on the gantry 3. And the degree of freedom of arrangement is improved. In addition, the activated carbon tank 7 and the ultraviolet sterilization tank 8 that require relatively maintenance and inspection of the device component 100 are disposed above the heat exchanger 101, and are located closer to the biological filtration tank 5 and the physical filtration tank 4. Maintenance is easy. Further, since the piping system 160 is attached to the gantry 3, the arrangement of the piping 200 (200a to 200l) is easy.

【0055】また、架台3の低い奥部3bには、水排出
部310が設けられ、この水排出部310にホース31
1が接続される。圧力式循環ろ過装置1から生じる結露
水が架台3の低い奥部3bに導かれ、この結露水は水排
出部310からホース311を介して排出され床に溢れ
ることがないようになっている。
Further, a water discharge portion 310 is provided in the lower inner portion 3 b of the gantry 3, and the water discharge portion 310 is connected to the hose 31.
1 is connected. The condensed water generated from the pressure-type circulating filtration device 1 is guided to the lower inner part 3b of the gantry 3, and the condensed water is discharged from the water discharge part 310 via the hose 311 and does not overflow to the floor.

【0056】生物ろ過槽5及び物理ろ過槽4の下流側
に、泡沫処理槽6が配置され、この生物ろ過槽5及び物
理ろ過槽4の上流側と泡沫処理槽6とを連通させるバイ
パス通路400を設けている。バイパス通路400には
熱交換器101が配置され、バイパス通路400の上流
側は切換弁300eを介して配管200bに接続され、
下流側は泡沫処理槽6の上部に接続されている。
A foam treatment tank 6 is disposed downstream of the biological filtration tank 5 and the physical filtration tank 4, and a bypass passage 400 for communicating the upstream of the biological filtration tank 5 and the physical filtration tank 4 with the foam treatment tank 6. Is provided. The heat exchanger 101 is disposed in the bypass passage 400, and the upstream side of the bypass passage 400 is connected to the pipe 200b via the switching valve 300e.
The downstream side is connected to the upper part of the foam treatment tank 6.

【0057】液体が配管200bから配管200cを介
して物理ろ過槽4側へ送られると共に、バイパス通路4
00、熱交換器101を介して泡沫処理槽6へ送られ、
この物理ろ過槽4側へ送られる流量と泡沫処理槽6へ送
られる流量が略同量となっており、液体をバイパス通路
400により泡沫処理槽6に導くことで総循環量を上げ
酸素供給量を増加することができる。また、生物ろ過槽
5及び/または物理ろ過槽4が仮に詰まることがあって
も、液体をバイパス通路400により泡沫処理槽6に導
いて循環させて酸素を供給することができる。また、バ
イパス通路400に熱交換器101を配置することで、
熱交換流量が増加して熱交換効率が向上する。
The liquid is sent from the pipe 200b to the physical filtration tank 4 via the pipe 200c,
00, sent to the foam treatment tank 6 via the heat exchanger 101,
The flow rate sent to the physical filtration tank 4 and the flow rate sent to the foam treatment tank 6 are substantially the same, and the liquid is guided to the foam treatment tank 6 through the bypass passage 400 to increase the total circulation amount and increase the oxygen supply amount. Can be increased. Also, even if the biological filtration tank 5 and / or the physical filtration tank 4 may be clogged, the liquid can be supplied to the foam treatment tank 6 through the bypass passage 400 and circulated to supply oxygen. Also, by disposing the heat exchanger 101 in the bypass passage 400,
The heat exchange flow rate increases and the heat exchange efficiency improves.

【0058】泡沫処理槽6の底部には、配管200kが
接続され、その配管200kの液体入口200k1は、
上部に位置している。泡沫処理槽6の側部には、水槽2
に戻すサージタンク26が備えられ、サージタンク26
の取り出し部26aから液体が配管200lを介して水
槽2へ戻される。
A pipe 200k is connected to the bottom of the foam treatment tank 6, and a liquid inlet 200k1 of the pipe 200k is
Located at the top. A water tank 2 is provided on the side of the foam treatment tank 6.
A surge tank 26 for returning to the
The liquid is returned to the water tank 2 from the take-out part 26a through the pipe 200l.

【0059】サージタンク26には、泡沫処理槽6内の
水を導く戻しパイプ27の上端開口が臨んでおり、この
戻しパイプ27の上端部には、上下方向へ移動可能なス
ライド管27aが接続され、スライド管27aを上下方
向へ移動することで、泡沫処理槽6内の液面レベルを容
易に調節することができる。また、戻しパイプ27の下
端部に形成された液体出口27bは、泡沫処理槽6内の
下部に位置している。液体が泡沫処理槽6の上部の液体
入口200k1から入り、下部の液体出口27bから取
り出すことで流れが複雑になり酸素の溶け込みを促すこ
とができる。
An upper end opening of a return pipe 27 for guiding water in the foam treatment tank 6 faces the surge tank 26, and a slide pipe 27 a that can move vertically is connected to the upper end of the return pipe 27. The liquid level in the foam treatment tank 6 can be easily adjusted by moving the slide tube 27a in the vertical direction. The liquid outlet 27 b formed at the lower end of the return pipe 27 is located at the lower part in the foam treatment tank 6. The liquid enters the liquid inlet 200k1 at the upper part of the foam treatment tank 6 and is taken out from the liquid outlet 27b at the lower part, whereby the flow becomes complicated and the dissolution of oxygen can be promoted.

【0060】不純物を泡沫状態の液体と共にオーバーフ
ローにより泡沫処理槽6の外部に除去する取出パイプ2
1は、泡沫処理槽6に回動可能に設けられている。取出
パイプ21の下端開口部21aの位置を変えることがで
きるようになっている。密閉部6aには、取出パイプ2
1の上端開口21bが位置しており、上端開口21bか
ら純物を泡沫状態の液体と共にオーバーフローにより泡
沫処理槽6の外部に除去する。
An extraction pipe 2 for removing impurities to the outside of the foam treatment tank 6 by overflowing together with the liquid in a foam state.
1 is rotatably provided in the foam processing tank 6. The position of the lower end opening 21a of the take-out pipe 21 can be changed. The extraction pipe 2 is provided in the sealing portion 6a.
The upper end opening 21b is located, and the pure substance is removed from the foam processing tank 6 from the upper end opening 21b together with the foamed liquid by overflow.

【0061】生物ろ過槽5及び物理ろ過槽4の内部の底
部にエアストーン500,501が配置され、このエア
ストーン500,501には逆止弁502,503を介
してエアホース504,505が接続され、このエアホ
ース504,505はエア分岐管105に接続されてい
る。エア分岐管105には、切換弁506,507が設
けられ、逆洗浄前に切換弁506,507を操作してエ
アポンプ104を駆動すると、エア分岐管105からエ
アホース504,505により構成されるエア通路から
逆止弁502,503を介して供給される。この空気
は、エアストーン500,501からエアレーションす
ることにより濾材の汚れを取り除き洗浄効率を向上させ
ることができる。
Air stones 500 and 501 are arranged at the bottom inside the biological filtration tank 5 and the physical filtration tank 4, and air hoses 504 and 505 are connected to the air stones 500 and 501 via check valves 502 and 503. The air hoses 504 and 505 are connected to the air branch pipe 105. Switching valves 506 and 507 are provided in the air branch pipe 105. When the switching valves 506 and 507 are operated to drive the air pump 104 before backwashing, an air passage formed by the air branch pipe 105 and the air hoses 504 and 505 is provided. Is supplied through the check valves 502 and 503. The air can be aerated from the air stones 500 and 501 to remove dirt from the filter medium and improve the washing efficiency.

【0062】エアストーン500、501には逆止弁5
02、503を介してエアホース504、505が接続
されており、逆止弁は、エアホース504、505から
エアストーン500、501への空気の流れを許容する
とともに、物理ろ過槽4及び生物ろ過槽5からエア分岐
管105及びエアポンプ104ヘの水の流れを阻止する
ように構成されているので、通常運転時(逆洗浄しない
時)にもエアホース504、505をエアストーン50
0、501に接続したままでよく便利である。
The air stones 500 and 501 have a check valve 5
The air hoses 504, 505 are connected via the air hoses 02, 503, and the check valves allow air to flow from the air hoses 504, 505 to the air stones 500, 501, and the physical filtration tank 4 and the biological filtration tank 5 The air hoses 504 and 505 are connected to the air stone 50 even during normal operation (when backwashing is not performed) since the water is prevented from flowing from the air branch pipe 105 and the air pump 104 to the air pump 104.
It is often convenient to keep it connected to 0,501.

【0063】エア分岐管105には切換弁510を介し
てエアホース511が接続され、エアホース511は切
換弁508を介して泡沫処理槽6の下部のエアストーン
512に接続され、泡沫処理槽6の下部に空気を供給
し、泡を発生させるエア源としている。
An air hose 511 is connected to the air branch pipe 105 via a switching valve 510, and the air hose 511 is connected to an air stone 512 below the foam processing tank 6 via a switching valve 508, and is connected to the lower part of the foam processing tank 6. Air is supplied to the air source to generate air bubbles.

【0064】[0064]

【発明の効果】前記したように、請求項1記載の発明
は、泡沫処理槽で形成される泡に液体に混入する不純物
が付着し、泡がさらに成長していくと取出手段によって
自動的に外部に除去することで、作業者の手作業によら
ないで、泡に付着して浮かぶ魚の体液等の不純物を泡と
共に自動的に除去することができ、衛生的である。
As described above, according to the first aspect of the present invention, impurities mixed into the liquid adhere to the foam formed in the foam treatment tank, and when the foam further grows, the extracting means automatically causes the foam to grow. By removing to the outside, impurities such as body fluids of fish that adhere to and float on the foam can be automatically removed together with the foam without the manual operation of the worker, which is sanitary.

【0065】請求項2記載の発明は、泡沫処理槽の上部
の密閉部の頂面が上方に凸形状の曲面であるから、成長
する泡が局部的に溜まることなく移動して円滑に、泡に
付着して浮かぶ魚の体液等の不純物を泡と共に自動的に
除去することができる。
According to the second aspect of the present invention, since the top surface of the sealing portion at the top of the foam treatment tank is a curved surface having an upwardly convex shape, the growing bubbles move smoothly without being locally collected, and the foam is smoothly moved. It is possible to automatically remove impurities such as body fluids of fish floating on the surface together with bubbles.

【0066】請求項3記載の発明は、泡沫処理槽の上部
の密閉部の頂面の少なくとも一部が透明部材で形成され
ているから、外部から容易に泡に付着して浮かぶ魚の体
液等の不純物を泡と共に自動的に除去する状態を確認す
ることができ、さらに密閉部の汚れも容易に確認するこ
とができる。
According to the third aspect of the present invention, since at least a part of the top surface of the sealing portion at the upper part of the foam treatment tank is formed of a transparent member, the body fluid of the fish or the like that easily adheres to the foam from the outside and floats. The state in which impurities are automatically removed together with the bubbles can be confirmed, and the contamination of the sealed portion can be easily confirmed.

【0067】請求項4記載の発明は、泡沫処理槽の上部
の密閉部の頂面の少なくとも一部が着脱可能であるか
ら、魚の体液等の不純物が集まり汚れ易い密閉部の頂面
を外して洗浄することができる。
According to the fourth aspect of the present invention, since at least a part of the top surface of the sealing portion at the top of the foam treatment tank is detachable, the top surface of the sealing portion where impurities such as fish body fluids are easily collected and contaminated is removed. Can be washed.

【0068】請求項5記載の発明は、泡沫処理槽内の液
体を導く戻しパイプを上下方向へ移動することで、泡沫
処理槽内の液面レベルを容易に調節することができ、除
去する魚の体液等の不純物の量を調整することができ
る。
According to the fifth aspect of the present invention, the level of the liquid in the foam treatment tank can be easily adjusted by moving the return pipe for guiding the liquid in the foam treatment tank in the vertical direction, and the fish to be removed can be adjusted. The amount of impurities such as body fluids can be adjusted.

【0069】請求項6記載の発明は、生物ろ過槽及び/
または物理ろ過槽と、請求項1乃至請求項5記載の泡沫
処理槽に、液体を加圧して循環させて液体に混入する不
純物を除去して浄化することができる。
The invention according to claim 6 is characterized in that a biological filtration tank and / or
Alternatively, the liquid can be pressurized and circulated through the physical filtration tank and the foam treatment tank according to the first to fifth aspects to remove impurities mixed in the liquid, thereby purifying the liquid.

【0070】請求項7記載の発明は、液体圧送手段を配
置して液体を圧送して泡沫処理槽、生物ろ過槽及び/ま
たは物理ろ過槽へ容易に循環させることができ、効率的
な液体の浄化が可能である。
According to the seventh aspect of the present invention, the liquid pumping means is arranged to pump the liquid and to easily circulate the liquid to the foam treatment tank, the biological filtration tank and / or the physical filtration tank, and to efficiently supply the liquid. Purification is possible.

【0071】請求項8記載の発明は、生物ろ過槽及び/
または物理ろ過槽に、循環方向とは逆方向へ液体を流す
簡単な構造で、かつ確実に生物ろ過槽及び/または物理
ろ過槽を清掃することができる。
The invention according to claim 8 is characterized in that a biological filtration tank and / or
Alternatively, the biological filtration tank and / or the physical filtration tank can be reliably cleaned with a simple structure in which the liquid flows in the physical filtration tank in a direction opposite to the circulation direction.

【0072】請求項9記載の発明は、液体をバイパス通
路により泡沫処理槽に導くことで総循環量を上げ酸素供
給量を増加することができる。また、生物ろ過槽及び/
または物理ろ過槽が仮に詰まることがあっても、液体を
バイパス通路により泡沫処理槽に導いて循環させて酸素
を供給することができる。
According to the ninth aspect of the present invention, by introducing the liquid to the foam treatment tank through the bypass passage, the total circulation amount can be increased and the oxygen supply amount can be increased. In addition, biological filtration tank and /
Alternatively, even if the physical filtration tank may be clogged, the liquid can be supplied to the foam treatment tank through the bypass passage and circulated to supply oxygen.

【0073】請求項10記載の発明は、液体が泡沫処理
槽の上部の液体入口から入り、下部の液体出口から取り
出すから、流れが複雑になり酸素の溶け込みを促すこと
ができる。
According to the tenth aspect of the present invention, since the liquid enters from the liquid inlet at the upper part of the foam treatment tank and is taken out from the liquid outlet at the lower part, the flow becomes complicated and the dissolution of oxygen can be promoted.

【0074】請求項11記載の発明は、逆洗浄前にエア
通路から空気を供給してエアレーションすることにより
濾材の汚れを取り除き洗浄効率を向上させることができ
る。
According to the eleventh aspect of the present invention, by supplying air from the air passage and performing aeration before backwashing, it is possible to remove dirt from the filter medium and improve the washing efficiency.

【0075】請求項12記載の発明は、架台に配管系を
取り付けることで、配管系が邪魔にならず架台に泡沫処
理槽、装置構成部品、生物ろ過槽及び物理ろ過槽をコン
パクトに配置することができる。さらに、架台の手前部
に操作系を集中して配置することで、保守、点検が容易
でメンテナンス性を向上させることができる。また、架
台に配管系を取り付けたから配管の配置が容易であり、
しかも架台で配管を隠すことができる。また、泡沫処理
槽、装置構成部品、生物ろ過槽及び物理ろ過槽がカバー
で覆われており、埃などから保護されると共に外観性が
向上する。
According to a twelfth aspect of the present invention, by attaching a piping system to the gantry, the piping system is not obstructed, and the foam treatment tank, the equipment components, the biological filtration tank and the physical filtration tank are compactly arranged on the gantry. Can be. Furthermore, by arranging the operation system in a concentrated manner in front of the gantry, maintenance and inspection are easy, and the maintainability can be improved. Also, since the piping system is attached to the gantry, piping arrangement is easy,
Moreover, the piping can be hidden by the mount. Further, the foam treatment tank, the component parts of the apparatus, the biological filtration tank, and the physical filtration tank are covered with a cover, so that the appearance is improved while being protected from dust and the like.

【0076】請求項13記載の発明は、液体の供給通路
と第1通賂とが連通した状態と、液体を外部に排出する
ドレン配管と第1通路とが連通した状態とを切り換え可
能に構成した第1切換え弁と、供給通路と第2通路とが
連通した状態と非連通との状態とを切り換え可能に構成
した第2切換え弁とを生物ろ過槽及び/または物理ろ過
槽の外部において互いに隣接させて配置したので、生物
ろ過槽及び/または物理ろ過槽に循環方向とは逆方向へ
液体を流して清掃する作業を簡単に行うことができる。
According to a thirteenth aspect of the present invention, a state in which the liquid supply passage and the first bribe are communicated with each other and a state in which the drain pipe for discharging the liquid to the outside and the first passage are communicated can be switched. A first switching valve and a second switching valve configured to be able to switch between a state in which the supply passage and the second passage are communicated and a state in which they are not communicated with each other outside the biological filtration tank and / or the physical filtration tank. Since they are arranged adjacent to each other, the cleaning operation can be easily performed by flowing the liquid through the biological filtration tank and / or the physical filtration tank in a direction opposite to the circulation direction.

【0077】請求項14記載の発明は、生物ろ過槽と物
理ろ過槽にそれぞれ設けた第1切換え弁と第2切換え弁
を、生物ろ過槽及び物理ろ過槽に対して同じ側に配置し
たので、生物ろ過槽と物理ろ過槽の第1切換え弁及び第
2切換え弁の切換え作業を容易に行え、生物ろ過槽と物
理ろ過槽を清掃する作業を簡単に行うことができる。
According to the fourteenth aspect of the present invention, the first switching valve and the second switching valve provided respectively in the biological filtration tank and the physical filtration tank are arranged on the same side with respect to the biological filtration tank and the physical filtration tank. The operation of switching between the first switching valve and the second switching valve between the biological filtration tank and the physical filtration tank can be easily performed, and the operation for cleaning the biological filtration tank and the physical filtration tank can be easily performed.

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

【図1】圧力式循環ろ過装置の第1実施例の平面図であ
る。
FIG. 1 is a plan view of a first embodiment of a pressure type circulation filtration device.

【図2】物理ろ過槽と泡沫処理槽の概略構成図である。FIG. 2 is a schematic configuration diagram of a physical filtration tank and a foam treatment tank.

【図3】生物ろ過槽の概略構成図である。FIG. 3 is a schematic configuration diagram of a biological filtration tank.

【図4】泡沫処理槽のエジェクタの断面図である。FIG. 4 is a sectional view of an ejector of the foam processing tank.

【図5】泡沫処理槽の上部の密閉部の他の実施例を示す
図である。
FIG. 5 is a view showing another embodiment of the closed portion at the top of the foam processing tank.

【図6】圧力式循環ろ過装置の第2実施例の平面図であ
る。
FIG. 6 is a plan view of a second embodiment of the pressure-type circulating filtration apparatus.

【図7】泡沫処理槽の概略構成図である。FIG. 7 is a schematic configuration diagram of a foam processing tank.

【図8】圧力式循環ろ過装置の第3実施例の平面図であ
る。
FIG. 8 is a plan view of a third embodiment of the pressure-type circulating filtration apparatus.

【図9】サイクロン装置とエジェクタトの概略構成図で
ある。
FIG. 9 is a schematic configuration diagram of a cyclone device and an ejecta.

【図10】圧力式循環ろ過装置の第4実施例の平面図で
ある。
FIG. 10 is a plan view of a fourth embodiment of the pressure-type circulation filtration device.

【図11】物理ろ過槽を洗浄する状態を示す図である。FIG. 11 is a diagram showing a state in which the physical filtration tank is washed.

【図12】生物ろ過槽を洗浄する状態を示す図である。FIG. 12 is a diagram showing a state in which the biological filtration tank is washed.

【図13】圧力式循環ろ過装置の第5実施例の正面図で
ある。
FIG. 13 is a front view of a fifth embodiment of the pressure-type circulating filtration apparatus.

【図14】圧力式循環ろ過装置の第5実施例の平面図で
ある。
FIG. 14 is a plan view of a fifth embodiment of the pressure-type circulating filtration apparatus.

【図15】圧力式循環ろ過装置の第5実施例の右側面図
である。
FIG. 15 is a right side view of a fifth embodiment of the pressure-type circulation filtration device.

【図16】圧力式循環ろ過装置の第5実施例の左側面図
である。
FIG. 16 is a left side view of a fifth embodiment of the pressure-type circulating filtration apparatus.

【図17】一部のカバーを外した状態の正面図である。FIG. 17 is a front view in a state where a part of a cover is removed.

【図18】一部のカバーを外した状態の平面図である。FIG. 18 is a plan view showing a state where some covers are removed.

【図19】一部のカバーを外した状態の右側面図であ
る。
FIG. 19 is a right side view with a part of the cover removed.

【図20】一部のカバーを外した状態の左側面図であ
る。
FIG. 20 is a left side view with a part of the cover removed.

【図21】圧力式循環ろ過装置の分解斜視図である。FIG. 21 is an exploded perspective view of a pressure-type circulation filtration device.

【符号の説明】[Explanation of symbols]

1 圧力式循環ろ過装置 4 物理ろ過槽 5 生物ろ過槽 6 泡沫処理槽 6a 密閉部 11 循環ポンプ 21 取出パイプ DESCRIPTION OF SYMBOLS 1 Pressure circulation filtration apparatus 4 Physical filtration tank 5 Biological filtration tank 6 Foam treatment tank 6a Sealing part 11 Circulation pump 21 Extraction pipe

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 3/06 ZAB C02F 9/00 502Z 9/00 501 B01D 35/02 C 502 35/14 101 ──────────────────────────────────────────────────の Continuation of the front page (51) Int.Cl. 6 Identification code Agency reference number FI Technical display location C02F 3/06 ZAB C02F 9/00 502Z 9/00 501 B01D 35/02 C 502 35/14 101

Claims (14)

【特許請求の範囲】[Claims] 【請求項1】液体を泡沫状態にして液体に混入する不純
物を除去する泡沫処理槽を備える圧力式循環ろ過装置に
おいて、前記泡沫処理槽の上部に密閉部を設け、さらに
前記密閉部に前記不純物を泡沫状態の液体と共に前記泡
沫処理槽の外部に除去する取出手段を設けたことを特徴
とする圧力式循環ろ過装置。
1. A pressure-type circulating filtration apparatus having a foam treatment tank for removing impurities mixed in a liquid by foaming the liquid, wherein a closed portion is provided at an upper portion of the foam treatment tank, and the impurity is further provided in the sealed portion. A pressure-type circulating filtration device provided with a take-out means for removing water from the foam treatment tank together with the foamed liquid.
【請求項2】前記密閉部の頂面を上方に凸形状の曲面に
形成したことを特徴とする請求項1記載の圧力式循環ろ
過装置。
2. The pressure-type circulating filtration device according to claim 1, wherein a top surface of the closed portion is formed as a curved surface having a convex shape upward.
【請求項3】前記密閉部の頂面の少なくとも一部を透明
部材で形成したことを特徴とする請求項1または請求項
2記載の圧力式循環ろ過装置。
3. The pressure-type circulating filtration device according to claim 1, wherein at least a part of a top surface of the closed portion is formed of a transparent member.
【請求項4】前記密閉部の頂面の少なくとも一部が着脱
可能であることを特徴とする請求項1乃至請求項3のい
ずれかに記載の圧力式循環ろ過装置。
4. The pressure-type circulating filtration device according to claim 1, wherein at least a part of a top surface of the sealing portion is detachable.
【請求項5】前記泡沫処理槽内の液体を上流側の液体タ
ンクに戻すサージタンクを備え、このサージタンクに前
記泡沫処理槽内の液体を導く戻しパイプを上下方向へ移
動可能に設けたことを特徴とする請求項1乃至請求項4
のいずれかに記載の圧力式循環ろ過装置。
5. A surge tank for returning a liquid in the foam processing tank to an upstream liquid tank, and a return pipe for guiding the liquid in the foam processing tank is provided in the surge tank so as to be movable in a vertical direction. 5. The method according to claim 1, wherein:
The pressure-type circulating filtration device according to any one of the above.
【請求項6】液体を洗浄する生物ろ過槽及び/または物
理ろ過槽と、前記請求項1乃至請求項5記載の泡沫処理
槽と、前記液体を加圧して前記生物ろ過槽及び/または
物理ろ過槽、密閉式泡沫処理槽に循環させる循環手段と
を備えることを特徴とする圧力式循環ろ過装置。
6. A biological filtration tank and / or a physical filtration tank for washing a liquid, the foam treatment tank according to any one of claims 1 to 5, and the biological filtration tank and / or a physical filtration tank by pressurizing the liquid. A pressure type circulating filtration device comprising: a tank; and a circulating means for circulating the liquid in the closed type foam treatment tank.
【請求項7】前記生物ろ過槽及び/または物理ろ過槽を
密閉式とし、この下流側に前記泡沫処理槽を配置し、さ
らに前記生物ろ過槽及び/または物理ろ過槽、前記泡沫
処理槽の上流側に前記液体を加圧して送る液体圧送手段
を配置したことを特徴とする請求項6記載の圧力式循環
ろ過装置。
7. The biofiltration tank and / or the physical filtration tank is hermetically sealed, and the foam treatment tank is arranged downstream of the biological filtration tank and / or the physical filtration tank. 7. A pressure-type circulating filtration device according to claim 6, wherein liquid pressure feeding means for feeding the liquid under pressure is arranged on the side.
【請求項8】前記生物ろ過槽及び/または物理ろ過槽
に、循環方向とは逆方向へ液体を流して清掃する液体流
路を設けたことを特徴とする請求項6または請求項7記
載の圧力式循環ろ過装置。
8. The biological filtration tank and / or the physical filtration tank is provided with a liquid flow path for cleaning by flowing a liquid in a direction opposite to a circulation direction. Pressure circulation filter.
【請求項9】生物ろ過槽及び/または物理ろ過槽の下流
側に、泡沫処理槽を配置し、液体を加圧して前記生物ろ
過槽及び/または物理ろ過槽、泡沫処理槽に循環させる
循環手段を備え、前記生物ろ過槽及び/または物理ろ過
槽の上流側と前記泡沫処理槽とを連通させるバイパス通
路を設けたことを特徴とする請求項1乃至請求項8のい
ずれかに記載の圧力式循環ろ過装置。
9. A circulating means for disposing a foam treatment tank downstream of the biological filtration tank and / or the physical filtration tank, and for pressurizing and circulating the liquid through the biological filtration tank and / or the physical filtration tank and the foam treatment tank. The pressure type according to any one of claims 1 to 8, further comprising: a bypass passage for communicating the upstream side of the biological filtration tank and / or the physical filtration tank with the foam treatment tank. Circulation filtration device.
【請求項10】前記泡沫処理槽の上部に液体入口を位置
させるとともに、下部に液体出口を位置させたことを特
徴とする請求項1乃至請求項9記載の圧力式循環ろ過装
置。
10. The pressure-type circulating filtration apparatus according to claim 1, wherein a liquid inlet is located at an upper part of the foam treatment tank, and a liquid outlet is located at a lower part.
【請求項11】前記生物ろ過槽及び/または物理ろ過槽
の内部の底部にエアストーンを配置し、このエアストー
ンに逆洗浄前にエアを供給するエア通路に逆止弁を設け
たことを特徴とする請求項1乃至請求項10記載の圧力
式循環ろ過装置。
11. An air stone is arranged at the bottom inside the biological filtration tank and / or the physical filtration tank, and a check valve is provided in an air passage for supplying air to the air stone before back washing. The pressure-type circulating filtration device according to any one of claims 1 to 10, wherein
【請求項12】架台に前記泡沫処理槽及びろ過槽以外の
装置構成部品を配置し、この奥部に前記生物ろ過槽及び
前記物理ろ過槽を配置し、手前部に操作系を集中して配
置し、さらに架台に配管系を取り付け、前記泡沫処理
槽、前記装置構成部品、前記生物ろ過槽及び前記物理ろ
過槽をカバーで覆ったことを特徴とする請求項1乃至請
求項11記載の圧力式循環ろ過装置。
12. An apparatus component other than the foam treatment tank and the filtration tank is arranged on a gantry, the biological filtration tank and the physical filtration tank are arranged in a deep part thereof, and an operation system is centrally arranged in a front part. The pressure system according to any one of claims 1 to 11, wherein a piping system is further attached to the gantry, and the foam treatment tank, the device components, the biological filtration tank, and the physical filtration tank are covered with a cover. Circulation filtration device.
【請求項13】前記液体流路は、前記生物ろ過槽及び/
または物理ろ過槽に液体を供給する第1通路と、前記生
物ろ過槽及び/または物理ろ過槽から液体を排出する第
2通路とで構成し、前記第1通路と第2通路を生物ろ過
槽及び/または物理ろ過槽の外部において互いに集合さ
せ、その集合部に液体の供給通路を接続する一方、前記
第1通路と第2通路にそれぞれ第1切換え弁と第2切換
え弁を前記生物ろ過槽及び/または物理ろ過槽の外部に
おいて互いに隣接させて配置し、前記第1切換え弁に液
体を外部に排出するドレン配管を接続し、前記第1切換
え弁は、前記供給通路と第1通路とが連通した状態と前
記第1通賂とドレン配管とが連通した状態とを切り換え
可能に構成し、前記第2切換え弁は、前記供給通路と第
2通路とが連通した状態と非連通との状態とを切り換え
可能に構成したことを特徴とする請求項8記載の圧力式
循環ろ過装置。
13. The method according to claim 13, wherein the liquid flow path includes the biological filtration tank and / or the biological filtration tank.
Or a first passage for supplying a liquid to the physical filtration tank, and a second passage for discharging the liquid from the biological filtration tank and / or the physical filtration tank, wherein the first passage and the second passage are formed by a biological filtration tank and And / or gathering each other outside the physical filtration tank and connecting a liquid supply passage to the gathering portion, and connecting a first switching valve and a second switching valve to the first passage and the second passage, respectively, with the biological filtration tank and And / or disposed adjacent to each other outside the physical filtration tank, and a drain pipe for discharging liquid to the outside is connected to the first switching valve, and the first switching valve connects the supply passage and the first passage. The state in which the supply passage and the second passage are communicated with each other and the state in which the supply passage and the second passage are communicated with each other can be switched between a state in which the supply passage and the drain passage communicate with each other. Is configured to be switchable. Pressure type circulation filtration system according to claim 8, wherein.
【請求項14】前記生物ろ過槽と物理ろ過槽を互いに隣
接して配置し、生物ろ過槽と物理ろ過槽にそれぞれ前記
第1切換え弁と第2切換え弁を設ける一方、これら第1
切換え弁と第2切換え弁を、前記生物ろ過槽及び物理ろ
過槽に対して同じ側に配置することを特徴とする請求項
13記載の圧力式循環ろ過装置。
14. The biological filtration tank and the physical filtration tank are disposed adjacent to each other, and the biological filtration tank and the physical filtration tank are provided with the first switching valve and the second switching valve, respectively.
14. The pressure-type circulating filtration device according to claim 13, wherein the switching valve and the second switching valve are arranged on the same side with respect to the biological filtration tank and the physical filtration tank.
JP9031538A 1996-02-16 1997-02-17 Pressure-type circulatory filter Pending JPH1066963A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9031538A JPH1066963A (en) 1996-02-16 1997-02-17 Pressure-type circulatory filter

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP2884996 1996-02-16
JP8-155843 1996-06-17
JP8-28849 1996-06-17
JP15584396 1996-06-17
JP9031538A JPH1066963A (en) 1996-02-16 1997-02-17 Pressure-type circulatory filter

Publications (1)

Publication Number Publication Date
JPH1066963A true JPH1066963A (en) 1998-03-10

Family

ID=27286340

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9031538A Pending JPH1066963A (en) 1996-02-16 1997-02-17 Pressure-type circulatory filter

Country Status (1)

Country Link
JP (1) JPH1066963A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0521558A2 (en) * 1991-07-02 1993-01-07 Koninklijke Philips Electronics N.V. Semiconductor device with means for increasing the breakdown voltage of a pn-junction
JP2006334568A (en) * 2005-06-06 2006-12-14 Taisei Corp Backwashing system
JP2011224422A (en) * 2010-04-15 2011-11-10 Yanmar Co Ltd Foam separation apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0521558A2 (en) * 1991-07-02 1993-01-07 Koninklijke Philips Electronics N.V. Semiconductor device with means for increasing the breakdown voltage of a pn-junction
JP2006334568A (en) * 2005-06-06 2006-12-14 Taisei Corp Backwashing system
JP4754884B2 (en) * 2005-06-06 2011-08-24 大成建設株式会社 Backwash system
JP2011224422A (en) * 2010-04-15 2011-11-10 Yanmar Co Ltd Foam separation apparatus

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