JP2930947B1 - Equipment for removing heavy metals from living organisms - Google Patents

Equipment for removing heavy metals from living organisms

Info

Publication number
JP2930947B1
JP2930947B1 JP10257766A JP25776698A JP2930947B1 JP 2930947 B1 JP2930947 B1 JP 2930947B1 JP 10257766 A JP10257766 A JP 10257766A JP 25776698 A JP25776698 A JP 25776698A JP 2930947 B1 JP2930947 B1 JP 2930947B1
Authority
JP
Japan
Prior art keywords
living body
tank
cathode
fat
electrolyte
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP10257766A
Other languages
Japanese (ja)
Other versions
JP2000083603A (en
Inventor
護 宮森
敏彦 丸山
雅夫 樋口
斎藤  弘
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.)
YUNIRETSUKUSU KK
Original Assignee
YUNIRETSUKUSU KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by YUNIRETSUKUSU KK filed Critical YUNIRETSUKUSU KK
Priority to JP10257766A priority Critical patent/JP2930947B1/en
Application granted granted Critical
Publication of JP2930947B1 publication Critical patent/JP2930947B1/en
Publication of JP2000083603A publication Critical patent/JP2000083603A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/34Treatment of water, waste water, or sewage with mechanical oscillations
    • C02F1/36Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4676Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electroreduction
    • C02F1/4678Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electroreduction of metals

Landscapes

  • General Preparation And Processing Of Foods (AREA)
  • Meat, Egg Or Seafood Products (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

【要約】 【課題】電解液に分散した油脂を電解槽に送出する前に
予め除去することにより、電解槽にて重金属の陽イオン
を効率良く陰極に析出できる。 【解決手段】生体11f内に重金属及び油脂が含まれる
生物体又はこの生体と重金属を溶解してイオン化する電
解液13とが浸漬槽14に貯留される。浸漬槽から送出
された電解液が油脂分離槽16に貯留され、この油脂分
離槽の下部に電解液に超音波振動を与える油脂凝集用振
動子42が設けられる。電解液面に浮上した油脂12が
油脂排出手段17により油脂分離槽から排出される。油
脂分離槽から送出された電解液が電解槽18に貯留さ
れ、この電解槽に陽極51及び陰極52が配設される。
陽極及び陰極に接続された直流電源53が陽極及び陰極
間に所定の電圧を印加して電解液中に溶出した重金属の
陽イオンを陰極に析出させ、電解槽の電解液は循環手段
56により浸漬槽に戻される。
Kind Code: A1 Abstract: By removing oils and fats dispersed in an electrolytic solution before sending it to an electrolytic cell, cations of heavy metals can be efficiently deposited on a cathode in the electrolytic cell. A living body in which a heavy metal and an oil or fat are contained in a living body or an electrolytic solution which dissolves and ionizes the living body and the heavy metal is stored in an immersion tank. The electrolyte delivered from the immersion tank is stored in the oil / fat separation tank 16, and a fat / oil aggregating vibrator 42 for applying ultrasonic vibration to the electrolyte is provided below the oil / fat separation tank. The grease 12 floating on the electrolyte surface is discharged from the grease separation tank by the grease discharging means 17. The electrolytic solution sent from the oil / fat separation tank is stored in the electrolytic tank 18, and an anode 51 and a cathode 52 are provided in the electrolytic tank.
A DC power supply 53 connected to the anode and the cathode applies a predetermined voltage between the anode and the cathode to deposit heavy metal cations eluted in the electrolyte on the cathode, and the electrolyte in the electrolytic cell is immersed by the circulation means 56. Returned to the tank.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、水産物、農産物等
の生物体の生体内に含まれる重金属を生物体から除去す
る装置に関する。更に詳しくは産業廃棄物として埋立て
処分されているホタテガイの生体に含まれるカドミウム
や鉛等の重金属を除去するのに適する装置に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for removing heavy metals contained in living organisms such as marine products and agricultural products from living organisms. More specifically, the present invention relates to an apparatus suitable for removing heavy metals such as cadmium and lead contained in living bodies of scallops that have been landfilled as industrial waste.

【0002】[0002]

【従来の技術】従来、この種の装置として、生体内に重
金属が含まれる生物体と電解液とが浸漬槽に貯留され、
陽極と陰極とが電解槽に所定の間隔をあけて配設され、
循環手段が浸漬槽の電解液を電解槽に送出しかつ電解槽
の電解液を浸漬槽に戻し、更に陽極と陰極とに電気的に
接続された直流電源が陽極及び陰極間に電圧を印加する
ように構成された、生物体に含まれる重金属を除去する
装置が開示されている(特開平9−47257号)。
2. Description of the Related Art Conventionally, as an apparatus of this type, a living body containing a heavy metal in a living body and an electrolyte are stored in an immersion tank.
An anode and a cathode are arranged at a predetermined interval in the electrolytic cell,
The circulating means sends the electrolytic solution in the immersion tank to the electrolytic cell and returns the electrolytic solution in the electrolytic tank to the immersion tank. Further, a DC power supply electrically connected to the anode and the cathode applies a voltage between the anode and the cathode. An apparatus configured to remove heavy metals contained in living organisms is disclosed (JP-A-9-47257).

【0003】このように構成された重金属を除去する装
置では、生物体の生体内に含まれる重金属は浸漬槽の電
解液に浸漬することにより徐々に電解液中に溶出して陽
イオンとなり、この陽イオンが溶出した電解液は循環手
段を介して電解槽に送出される。電解槽の陽極と陰極に
直流電圧を印加すると、陽イオンとなった重金属が陰極
に析出し、電解槽中の電解液から陽イオンとなった重金
属が除去されて循環手段を介して浸漬槽に戻される。こ
の結果、生物体からの重金属の除去率が極めて高くな
り、処理後の生物体の水洗は短時間で済み、また生物体
の処理量の増大に伴う操作を簡単に行うことができるよ
うになっている。
[0003] In the apparatus for removing heavy metals configured as described above, heavy metals contained in the living body of a living organism are gradually eluted into the electrolyte by immersion in the electrolyte in an immersion tank to become cations. The electrolytic solution from which the cations have been eluted is sent out to the electrolytic cell via the circulation means. When a DC voltage is applied to the anode and the cathode of the electrolytic cell, the cation heavy metal is deposited on the cathode, and the cation heavy metal is removed from the electrolytic solution in the electrolytic cell, and the cation is transferred to the immersion tank via the circulation means. Will be returned. As a result, the removal rate of heavy metals from living organisms becomes extremely high, and washing of living organisms after treatment can be performed in a short time, and operations associated with an increase in the throughput of living organisms can be performed easily. ing.

【0004】[0004]

【発明が解決しようとする課題】しかし、上記従来の特
開平9−47257号公報に示された生物体に含まれる
重金属を除去する装置では、浸漬槽において電解液に重
金属の陽イオンが溶出するとともに、生物体の生体内に
含まれる油脂が生物体から離脱して電解液に分散し、こ
の油脂が電解槽の陽極及び陰極表面に付着する場合があ
った。この結果、電解に寄与する陽極及び陰極の表面積
が減少し、電解液中の電流密度が低下するため、重金属
の陽イオンの陰極への析出量が低下する問題点があっ
た。本発明の目的は、電解液に分散した油脂を電解槽に
送出する前に予め除去することにより、電解槽にて重金
属の陽イオンを効率良く陰極に析出できる、生物体に含
まれる重金属の除去装置を提供することにある。
However, in the apparatus for removing heavy metals contained in living organisms described in the above-mentioned conventional Japanese Patent Application Laid-Open No. 9-47257, cations of heavy metals are eluted into the electrolyte in an immersion tank. At the same time, the fats and oils contained in the living body of the living body may be separated from the living body and dispersed in the electrolytic solution, and this fat and oil may adhere to the anode and cathode surfaces of the electrolytic cell. As a result, the surface area of the anode and the cathode contributing to the electrolysis is reduced, and the current density in the electrolytic solution is reduced, so that the amount of heavy metal cations deposited on the cathode is reduced. An object of the present invention is to remove heavy metals contained in living organisms by removing fats and oils dispersed in an electrolytic solution in advance before sending them to an electrolytic cell, whereby cations of heavy metals can be efficiently deposited on a cathode in the electrolytic cell. It is to provide a device.

【0005】[0005]

【課題を解決するための手段】請求項1に係る発明は、
図1及び図3に示すように、生体11f内に重金属及び
油脂12が含まれる生物体11又は上記生体11fと重
金属を溶解してイオン化する硫酸溶液、塩酸溶液、水酸
化ナトリウム溶液又は塩化ナトリウム溶液からなる電解
液13とが貯留された浸漬槽14と、浸漬槽14から送
出された電解液13が貯留されかつ生物体11又は生体
11fから離脱して分散する油脂12を含む電解液13
に超音波振動を与える油脂凝集用振動子42が底部に設
けられた油脂分離槽16と、油脂分離槽16の上部に設
けられ油脂凝集用振動子42により電解液13面に浮上
した油脂12を油脂分離槽16から排出する油脂排出手
段17と、油脂分離槽16から送出された電解液13が
貯留されかつ陽極51及び陰極52が所定の間隔をあけ
て配設された電解槽18と、陽極51及び陰極52に電
気的に接続され陽極51及び陰極52間に所定の電圧を
印加して電解液13中に溶出した重金属の陽イオンを陰
極52に析出させる直流電源53と、浸漬槽14の電解
液13を油脂分離槽16を介して電解槽18に送出し電
解槽18の電解液13を浸漬槽14に戻す循環手段56
とを備えた生物体に含まれる重金属の除去装置である。
The invention according to claim 1 is
As shown in FIG. 1 and FIG. 3, a living body 11 f containing a heavy metal and an oil or fat 12 in a living body 11 f or a sulfuric acid solution, a hydrochloric acid solution, a sodium hydroxide solution or a sodium chloride solution in which the living body 11 f and the heavy metal are dissolved and ionized. Immersion tank 14 in which electrolytic solution 13 is stored, and electrolytic solution 13 containing oil 12 in which electrolytic solution 13 delivered from immersion tank 14 is stored and separated from biological body 11 or living body 11f and dispersed.
The oil / fat separation tank 16 provided at the bottom with a fat / oil aggregating element 42 for applying ultrasonic vibration to the oil / fat separation tank 16 and the oil / fat 12 floated on the surface of the electrolyte 13 by the oil / fat aggregating element 42 provided on the top of the oil / fat separation tank 16 An oil / fat discharging means 17 for discharging the oil / fat separating tank 16, an electrolytic tank 18 in which the electrolytic solution 13 sent out from the oil / fat separating tank 16 is stored, and an anode 51 and a cathode 52 are arranged at a predetermined interval; A direct current power supply 53 electrically connected to the cathode 51 and the cathode 52 to apply a predetermined voltage between the anode 51 and the cathode 52 to deposit cations of heavy metals eluted in the electrolytic solution 13 on the cathode 52; Circulating means 56 for sending the electrolytic solution 13 to the electrolytic bath 18 via the oil / fat separating bath 16 and returning the electrolytic solution 13 in the electrolytic bath 18 to the immersion bath 14
This is a device for removing heavy metals contained in living organisms comprising:

【0006】この請求項1に記載された重金属の除去装
置では、生体11f内に含まれる重金属は浸漬槽14の
電解液13に浸漬することにより徐々に電解液13中に
溶出して陽イオンとなり、また生体11f内に含まれる
油脂12は電解液13に分散し、この陽イオンが溶出し
かつ油脂が分散した電解液13は循環手段56により油
脂分離槽16に送出される。この電解液13には油脂凝
集用振動子42により超音波振動が与えられ、電解液1
3中の油脂12が凝集して電解液13表面に浮上する。
電解液13表面に浮上した油脂12は油脂排出手段17
により油脂分離槽16から排出され、油脂12が除去さ
れた電解液13は電解槽18に送出される。電解槽18
では直流電源53により陽極51及び陰極52間に所定
の電圧が印加され、電解液13中の重金属の陽イオンが
陰極52に析出して除去される。この電解液13は循環
手段56により浸漬槽14に戻される。
In the apparatus for removing heavy metals according to the first aspect, the heavy metals contained in the living body 11f are gradually eluted into the electrolyte 13 by being immersed in the electrolyte 13 in the immersion tank 14, and become cations. The fats and oils 12 contained in the living body 11f are dispersed in the electrolyte solution 13, and the cations are eluted and the electrolyte solution 13 in which the fats and oils are dispersed is sent out to the fat and oil separation tank 16 by the circulation means 56. Ultrasonic vibration is applied to the electrolyte 13 by a vibrator 42 for agglomeration of fats and oils.
The fats and oils 12 in 3 are agglomerated and float on the surface of the electrolyte 13.
The grease 12 floating on the surface of the electrolyte 13 is
The electrolytic solution 13 discharged from the oil / fat separation tank 16 from which the oil / fat 12 has been removed is sent to the electrolytic tank 18. Electrolyzer 18
In this case, a predetermined voltage is applied between the anode 51 and the cathode 52 by the DC power supply 53, and heavy metal cations in the electrolytic solution 13 are deposited on the cathode 52 and removed. The electrolytic solution 13 is returned to the immersion tank 14 by the circulation means 56.

【0007】請求項2に係る発明は、請求項1に係る発
明であって、更に図1及び図3に示すように、浸漬槽1
4の底部に生物体11又は生体11fに超音波振動を与
える浸透用振動子32が設けられたことを特徴とする。
この請求項2に記載された重金属の除去装置では、浸透
用振動子32により浸漬槽14内の生物体11又は生体
11fに超音波振動が与えられるので、電解液13が生
物体11又は生体11fに速やかに浸透し、生物体11
又は生体11f内に含まれる重金属が陽イオンとなって
速やかに電解液13に溶出し、更に生物体11又は生体
11f内の油脂12が生体11fから離脱して電解液1
3に分散する。
[0007] The invention according to claim 2 is the invention according to claim 1, and further includes an immersion tank 1 as shown in FIGS.
4 is characterized in that a penetrating vibrator 32 for applying ultrasonic vibration to the living body 11 or the living body 11f is provided at the bottom of the living body 11.
In the heavy metal removing apparatus according to the second aspect, since the ultrasonic vibration is applied to the living body 11 or the living body 11f in the immersion tank 14 by the permeation vibrator 32, the electrolytic solution 13 is supplied to the living body 11 or the living body 11f. Quickly penetrate into the organism 11
Alternatively, heavy metals contained in the living body 11f become cations and are quickly eluted into the electrolytic solution 13, and furthermore, the fats and oils 12 in the living body 11 or the living body 11f are separated from the living body 11f and the electrolyte 1
Disperse into 3.

【0008】請求項3に係る発明は、請求項1又は2に
係る発明であって、更に図1又は図9に示すように、電
解槽18の底部又は陰極82の下面に陰極52又は82
に超音波振動を与える電極洗浄用振動子54又は94が
設けられたことを特徴とする。この請求項3に記載され
た重金属の除去装置では、電極洗浄用振動子54又は9
4により陽極51及び陰極52又は陰極82に超音波振
動が与えられるので、陽極51及び陰極52表面又は陰
極82表面に付着した油脂12や水素の気泡が速やかに
陽極51及び陰極52又は陰極82から離脱し、陽極5
1及び陰極52又は陰極82の表面は常に清浄な状態に
保たれる。
The invention according to claim 3 is the invention according to claim 1 or 2, wherein the cathode 52 or 82 is provided on the bottom of the electrolytic cell 18 or the lower surface of the cathode 82, as shown in FIG. 1 or FIG.
The electrode cleaning vibrator 54 or 94 for applying ultrasonic vibration to the electrode cleaning device. In the heavy metal removing apparatus according to the third aspect, the electrode cleaning vibrator 54 or 9 is used.
4. Ultrasonic vibration is applied to the anode 51 and the cathode 52 or the cathode 82 by 4, so that the oil 12 or hydrogen bubbles adhered to the surface of the anode 51 and the cathode 52 or the surface of the cathode 82 are quickly discharged from the anode 51 and the cathode 52 or the cathode 82. Detached, anode 5
1 and the surface of the cathode 52 or the cathode 82 are always kept clean.

【0009】請求項4に係る発明は、請求項1ないし3
いずれか記載の発明であって、更に図1〜図3に示すよ
うに、浸漬槽14が生物体11又は生体11fの搬送方
向に沿って延びて形成され、生物体11又は生体11f
が複数のバケット25に収容され、複数のバケット25
が搬送手段26により所定の間隔をあけて生物体11又
は生体11fの搬送方向に沿って搬送され、複数のバケ
ット25の搬送時に複数のバケット25内の生物体11
又は生体11fが浸漬槽14の電解液13に浸漬される
ように構成されたことを特徴とする。この請求項4に記
載された重金属の除去装置では、生物体11又は生体1
1fからの重金属除去処理や、生物体11又は生体11
fの脱脂処理を連続的にかつ自動的に行うことができ、
大量の生物体11又は生体11fを処理するのに適す
る。
The invention according to claim 4 is the invention according to claims 1 to 3
In any of the inventions described above, as further shown in FIGS. 1 to 3, the immersion tank 14 is formed to extend along the transport direction of the living body 11 or the living body 11 f, and the living body 11 or the living body 11 f is formed.
Are stored in the plurality of buckets 25, and the plurality of buckets 25
Are transported along the transport direction of the living body 11 or the living body 11 f at predetermined intervals by the transporting means 26, and when the plurality of buckets 25 are transported, the living organisms 11 in the plurality of buckets 25 are transported.
Alternatively, the living body 11f is configured to be immersed in the electrolytic solution 13 of the immersion tank 14. In the apparatus for removing heavy metals according to the fourth aspect, the living body 11 or the living body 1 is removed.
1f to remove the heavy metal from the living body 11 or the living body 11
f can be performed continuously and automatically,
It is suitable for treating a large amount of the living body 11 or the living body 11f.

【0010】請求項5に係る発明は、請求項1ないし3
いずれかに係る発明であって、更に図7に示すように、
生物体又は生体11fがバケット75に収容され、バケ
ット75がバケット昇降手段71により浸漬槽74に挿
入されかつ引上げられ、バケット75の浸漬槽74への
挿入時にバケット75内の生物体又は生体11fが浸漬
槽74の電解液13に浸漬されるように構成されたこと
を特徴とする。この請求項5に記載された重金属の除去
装置では、生物体又は生体11fからの重金属除去処理
や、生物体又は生体11fの脱脂処理を少ない量の電解
液13で行うことができ、少量の生物体又は生体11f
を処理するのに適する。
The invention according to claim 5 is the invention according to claims 1 to 3
The invention according to any of the above, and as shown in FIG.
The organism or living body 11f is accommodated in a bucket 75, and the bucket 75 is inserted into the immersion tank 74 by the bucket elevating means 71 and pulled up. When the bucket 75 is inserted into the immersion tank 74, the organism or living body 11f in the bucket 75 is removed. The immersion tank 74 is characterized by being immersed in the electrolyte 13. In the heavy metal removal apparatus according to the fifth aspect, the heavy metal removal treatment from the living body or the living body 11f and the defatting treatment of the living body or the living body 11f can be performed with a small amount of the electrolytic solution 13. Body or living body 11f
Suitable for processing.

【0011】[0011]

【発明の実施の形態】次に本発明の実施の形態を図面に
基づいて説明する。生体内に重金属を含む生物体として
はホタテガイ、イカ等の魚貝類(水産物)や、動物、農
産物又は植物等の生物体を挙げることができ、重金属と
してはカドミウム、鉛、ヒ素、水銀、銅、亜鉛、ニッケ
ル、クロム、マンガン、コバルト等の重金属を挙げるこ
とができる。また重金属を含む生体としては、ホタテガ
イやイカの魚貝類等の臓物、例えば図3に示すホタテガ
イ11の生体11fとしては、ウロと呼ばれる中腸腺1
1cや貝柱11a側面に付着する腎臓11e等を挙げる
ことができる。なお、図3の符号11bは靱帯であり、
符号11dはヒモと呼ばれる外套膜である。図1に示す
ように、重金属の除去装置10は重金属及び油脂12が
含まれる生体11fと重金属を溶解してイオン化する電
解液13とが貯留された浸漬槽14と、浸漬槽14から
送出された電解液13が貯留された油脂分離槽16と、
油脂分離槽16の上部に設けられた油脂排出手段17
と、油脂分離槽16から送出された電解液13が貯留さ
れた電解槽18とを備える。
Embodiments of the present invention will now be described with reference to the drawings. Organisms containing heavy metals in the living body include scallops, fish and shellfish (marine products) such as squid, and organisms such as animals, agricultural products or plants. Heavy metals include cadmium, lead, arsenic, mercury, copper, and the like. Examples include heavy metals such as zinc, nickel, chromium, manganese, and cobalt. In addition, as a living body containing a heavy metal, a scallop or a squid fish and shellfish, etc., for example, a living body 11f of a scallop 11 shown in FIG.
1c and a kidney 11e attached to the side surface of the scallop 11a. Note that reference numeral 11b in FIG. 3 denotes a ligament,
Reference numeral 11d denotes a mantle called a string. As shown in FIG. 1, the heavy metal removing device 10 is delivered from an immersion tank 14 in which a living body 11 f containing heavy metals and fats and oils 12 and an electrolytic solution 13 for dissolving and ionizing heavy metals are stored, and an immersion tank 14. An oil / fat separation tank 16 in which an electrolyte 13 is stored;
Oil / fat discharge means 17 provided at the top of oil / fat separation tank 16
And an electrolytic tank 18 in which the electrolytic solution 13 sent from the oil / fat separating tank 16 is stored.

【0012】浸漬槽14は生体11fの搬送方向に沿っ
て延びて形成され、浸漬槽14のバケット出口14aに
は第1水切り板21を介して浸漬槽14と略同一形状に
形成された洗浄槽19のバケット入口19aが接続され
る(図2)。洗浄槽19には水23又は中和剤が貯留さ
れ、洗浄槽19のバケット出口19bには第2水切り板
22が設けられる。生体11fは複数のバケット25に
収容され(図1及び図2)、これらのバケット25は電
解液13及び水23又は中和剤が通過可能にかつ生体1
1fが通過不能に網状又は格子状に形成された籠であ
り、底網25aが開閉可能に構成される。また浸漬槽1
4の上方にはこの浸漬槽14の長手方向に沿ってバケッ
ト25を所定の間隔をあけて搬送可能な搬送手段26が
設けられる。搬送手段26はこの実施の形態ではリフト
式コンベヤであり、生体11fの搬送方向に沿って設け
られた伏せC字状のレール27と、このレール27内を
転動可能な複数の軸付ローラ28と、これらの軸付ロー
ラ28の軸部28aから垂下されたフック29と、複数
の軸部28aを所定の間隔をあけて連結するチェーン3
1とを有する。
The immersion tank 14 is formed so as to extend along the transport direction of the living body 11f, and a washing tank formed in a bucket outlet 14a of the immersion tank 14 through the first draining plate 21 to have substantially the same shape as the immersion tank 14. Nineteen bucket inlets 19a are connected (FIG. 2). Water 23 or a neutralizing agent is stored in the washing tank 19, and a second drain plate 22 is provided at a bucket outlet 19 b of the washing tank 19. The living body 11f is housed in a plurality of buckets 25 (FIGS. 1 and 2), and these buckets 25 allow the electrolyte 13 and water 23 or a neutralizing agent to pass therethrough and the living body 1
1f is a basket formed in a mesh or lattice shape so as not to pass, and the bottom net 25a is configured to be openable and closable. Dipping tank 1
A transporting means 26 capable of transporting the bucket 25 at predetermined intervals along the longitudinal direction of the immersion tank 14 is provided above the immersion tank 14. The transporting means 26 is a lift type conveyor in this embodiment, and has a protruding C-shaped rail 27 provided along the transporting direction of the living body 11f, and a plurality of shafted rollers 28 which can roll inside the rail 27. And a chain 3 for connecting the plurality of shaft portions 28a at predetermined intervals to hooks 29 suspended from the shaft portions 28a of these shaft-mounted rollers 28.
And 1.

【0013】レール27は長円状に形成され、浸漬槽1
4及び洗浄槽19の上方に設けられた往路部27a(図
2)と、浸漬槽14及び洗浄槽19の上方から外れた位
置に往路部27aとほぼ平行に設けられた復路部(図示
せず)と、往路部27a及び復路部の両端を連結する一
対の連結部(図示せず)とからなる。往路部27aには
浸漬槽14及び洗浄槽19のバケット入口14a,19
aに対向して第1及び第2下り傾斜部27b,27cが
それぞれ形成され、浸漬槽14及び洗浄槽19のバケッ
ト出口14b,19bに対向して第1及び第2登り傾斜
部27d,27eがそれぞれ形成される。また第1下り
傾斜部27bと第1登り傾斜部27dとの間には第1ロ
ア水平部27fが形成され、第2下り傾斜部27cと第
2登り傾斜部27eとの間には第2ロア水平部27gが
形成される。図2の符号27h,27i及び27jは第
1、第2及び第3アッパ水平部である。また複数のフッ
ク29には複数のバケット25がそれぞれ吊下げられ、
チェーン31は図示しないが駆動スプロケットを介して
減速機付モータにより駆動される。これにより軸付ロー
ラ28がレール27の内面を転動し、フック29に吊下
げられたバケット25が所定の間隔をあけかつ所定の速
度で生体11fの搬送方向に沿って搬送されるように構
成される。なお、上記搬送速度はバケット25内の生体
11fの電解液13への浸漬時間が4〜24時間になる
ように設定される。
The rail 27 is formed in an oval shape, and
4 and a forward path 27a (FIG. 2) provided above the cleaning tank 19, and a return path (not shown) provided at a position deviated from above the immersion tank 14 and the cleaning tank 19 and substantially parallel to the forward path 27a. ) And a pair of connecting portions (not shown) for connecting both ends of the outward path portion 27a and the return path portion. In the forward path 27a, the bucket inlets 14a, 19 of the immersion tank 14 and the cleaning tank 19 are provided.
The first and second downward slopes 27b and 27c are formed opposite to the first and second downward slopes 27d and 27e, respectively, facing the immersion tank 14 and the bucket outlets 14b and 19b of the washing tank 19. Each is formed. Further, a first lower horizontal portion 27f is formed between the first descending inclined portion 27b and the first climbing inclined portion 27d, and a second lower horizontal portion is formed between the second descending inclined portion 27c and the second climbing inclined portion 27e. A horizontal portion 27g is formed. Reference numerals 27h, 27i and 27j in FIG. 2 denote first, second and third upper horizontal portions. Also, a plurality of buckets 25 are suspended from a plurality of hooks 29, respectively.
Although not shown, the chain 31 is driven by a motor with a speed reducer via a driving sprocket. Thereby, the roller 28 with a shaft rolls on the inner surface of the rail 27, and the bucket 25 suspended by the hook 29 is transported at a predetermined interval and at a predetermined speed along the transport direction of the living body 11f. Is done. The transport speed is set so that the immersion time of the living body 11f in the bucket 25 in the electrolyte 13 is 4 to 24 hours.

【0014】浸漬槽14の底部には生体11fに超音波
振動を与える複数の浸透用振動子32が所定の間隔をあ
けて設けられる。これらの浸透用振動子32は図5に詳
しく示すように、一対の腕部32a,32aを有し、磁
歪型又はπ型と呼ばれる略逆U字状のフェライト振動子
である。この振動子32の上面にはエキスポーネンシャ
ルホーン33が貼着され、このホーン33の先端が振動
板34に接触するように構成される。また振動子32の
一対の腕部32a,32aにはコイル36が巻回され、
一対の腕部32a,32a間にはバイアス用磁石37が
挿入される。コイル36は超音波用電源38に接続され
る、即ち整合回路38a、出力回路38b、超音波発振
回路38c及び電源回路38dを介して交流電源に接続
される。上記超音波発振回路38c及び出力回路38b
にてコイル36への発振周波数及び出力がそれぞれ調整
可能に構成される。発振周波数及び出力が調整された電
流がコイル36に流れると、振動子32に上記電流に応
じた交番磁界が発生し、振動板34を介して電解液13
中の生体11fに所定の周波数及び所定の振幅で超音波
振動を与えるように構成される。なお、超音波振動の周
波数は18kHz〜60kHzの範囲に設定され、その
電力は0.5〜4kW/cm2の範囲に設定されること
が好ましい。
At the bottom of the immersion tank 14, a plurality of penetrating vibrators 32 for applying ultrasonic vibration to the living body 11f are provided at predetermined intervals. As shown in detail in FIG. 5, these penetrating vibrators 32 are a pair of arm portions 32a, 32a, and are substantially inverted U-shaped ferrite vibrators called magnetostrictive or π-type. An exponential horn 33 is adhered to the upper surface of the vibrator 32, and the tip of the horn 33 is configured to contact the diaphragm 34. A coil 36 is wound around the pair of arms 32a, 32a of the vibrator 32,
A biasing magnet 37 is inserted between the pair of arms 32a. The coil 36 is connected to an ultrasonic power supply 38, that is, to an AC power supply via a matching circuit 38a, an output circuit 38b, an ultrasonic oscillation circuit 38c, and a power supply circuit 38d. The ultrasonic oscillation circuit 38c and the output circuit 38b
, The oscillation frequency and output to the coil 36 can be adjusted. When a current whose oscillation frequency and output have been adjusted flows through the coil 36, an alternating magnetic field corresponding to the current is generated in the vibrator 32, and the electrolyte 13 flows through the vibrating plate 34.
It is configured to apply ultrasonic vibration to the inside living body 11f at a predetermined frequency and a predetermined amplitude. Preferably, the frequency of the ultrasonic vibration is set in a range of 18 kHz to 60 kHz, and the power thereof is set in a range of 0.5 to 4 kW / cm 2 .

【0015】一方、洗浄槽19の底部にも生体11fに
超音波振動を与える生体洗浄用振動子39が所定の間隔
をあけて設けられる(図2)。生体洗浄用振動子39は
上記浸透用振動子32と同一に構成され、上記と同様に
超音波用電源38に接続される(図5)。また洗浄槽1
9のバケット出口19b近傍にはスクリューコンベヤ4
1が設けられる。このコンベヤ41はバケット25から
落下した生体11fを受けるホッパ部41aと、ホッパ
部41aに連設され水平に延びるガイド筒41bと、ガ
イド筒41bに回転可能に挿入された軸部41cと、軸
部41cの外周面に螺旋状に固着された羽根部41d
と、軸部41cを駆動するモータ部41eとを有する。
On the other hand, a living body washing vibrator 39 for applying ultrasonic vibration to the living body 11f is also provided at a predetermined interval at the bottom of the washing tank 19 (FIG. 2). The living body vibrator 39 has the same configuration as the permeation vibrator 32, and is connected to the ultrasonic power supply 38 in the same manner as described above (FIG. 5). Cleaning tank 1
9 near the bucket outlet 19b.
1 is provided. The conveyor 41 includes a hopper 41a for receiving the living body 11f dropped from the bucket 25, a guide cylinder 41b connected to the hopper 41a and extending horizontally, a shaft 41c rotatably inserted into the guide cylinder 41b, and a shaft. 41d spirally fixed to the outer peripheral surface of 41c
And a motor section 41e for driving the shaft section 41c.

【0016】電解液13としては硫酸溶液、水酸化ナト
リウム溶液、塩化ナトリウム溶液、塩酸溶液又は硝酸溶
液等を挙げることができる。電解液13として硫酸溶液
を用いた場合、この硫酸溶液の濃度は0.5〜20容量
%、好ましくは1〜3容量%の範囲内に設定される。濃
度を0.5〜20容量%としたのは、濃度が0.5容量
%未満では生体11f内に含まれる重金属を効率的に陰
極52(図1)に析出できず、また濃度が20容量%を
越えると上記生体11fが変質したり、重金属を除去し
た後の生体11fの中和処理に多くの時間を要する不具
合があるからである。なお、電解液13の温度は常温〜
40℃の範囲に設定されることが好ましい。40℃を越
えると生体11fが煮えてしまうためである。また洗浄
槽19に水23ではなく中和剤を貯留する場合には、酸
性の電解液に対してはアルカリ性の中和剤が用いられ、
アルカリ性の電解液に対しては酸性の中和剤が用いられ
る。
Examples of the electrolyte 13 include a sulfuric acid solution, a sodium hydroxide solution, a sodium chloride solution, a hydrochloric acid solution and a nitric acid solution. When a sulfuric acid solution is used as the electrolytic solution 13, the concentration of the sulfuric acid solution is set in the range of 0.5 to 20% by volume, preferably 1 to 3% by volume. The reason why the concentration is set to 0.5 to 20% by volume is that if the concentration is less than 0.5% by volume, heavy metals contained in the living body 11f cannot be efficiently deposited on the cathode 52 (FIG. 1), and the concentration is 20% by volume. %, There is a problem that the living body 11f is degraded, and a long time is required for the neutralization treatment of the living body 11f after removing heavy metals. In addition, the temperature of the electrolytic solution 13 is from room temperature to
It is preferable that the temperature is set in the range of 40 ° C. If the temperature exceeds 40 ° C., the living body 11f is boiled. When a neutralizing agent is stored in the washing tank 19 instead of the water 23, an alkaline neutralizing agent is used for an acidic electrolytic solution,
An acidic neutralizing agent is used for an alkaline electrolyte.

【0017】油脂分離槽16の下部には生体11fから
離脱して分散する油脂12を含む電解液13に超音波振
動を与える油脂凝集用振動子42が設けられる(図
1)。この振動子42は上記浸透用振動子32と略同一
に構成され、上記と同様に超音波用電源38に接続され
る(図5)。この振動子42により油脂分離槽16内の
電解液13に所定の周波数及び所定の振幅で超音波振動
が与えられ、電解液13中に分散している油脂12を凝
集するように構成される。図1の符号43は油脂分離槽
16内に設けられ超音波振動を効率良く電解液13に伝
搬させる反射板である。
At the lower part of the oil / fat separating tank 16, there is provided a vibrator 42 for aggregating oil / fat which applies ultrasonic vibration to the electrolyte 13 containing the oil / fat 12 separated from the living body 11f and dispersed therein (FIG. 1). The vibrator 42 has substantially the same configuration as the penetrating vibrator 32, and is connected to the ultrasonic power supply 38 as described above (FIG. 5). Ultrasonic vibration is applied to the electrolyte 13 in the oil / fat separation tank 16 at a predetermined frequency and a predetermined amplitude by the vibrator 42, and the oil / fat 12 dispersed in the electrolyte 13 is aggregated. Reference numeral 43 in FIG. 1 is a reflection plate provided in the oil / fat separation tank 16 for efficiently transmitting ultrasonic vibrations to the electrolyte 13.

【0018】油脂排出手段17は下端が油脂分離槽16
の電解液13の液面に接し上端が油脂回収槽44に臨む
ように傾斜して設けられたベルトコンベヤ46と、この
コンベヤ46のベルト46c外周面に所定の間隔をあけ
て突設された多数のスキーマ47と、上記コンベヤ46
と同一角度で傾斜し油脂分離槽16の略中央から油脂回
収槽44の上方に延びるガイド板48とを有する(図
1)。ベルトコンベヤ46は油脂回収槽16の上方に設
けられ減速機付モータ(図示せず)により駆動される駆
動プーリ46aと、油脂分離槽16の電解液13面に接
するように設けられた従動プーリ46bと、これらのプ
ーリ46a,46bに掛け渡された無端のベルト46c
とからなる。
The lower end of the oil / fat discharging means 17 is
A belt conveyor 46 which is in contact with the liquid surface of the electrolytic solution 13 and whose upper end is inclined so as to face the oil / fat recovery tank 44, and a number of belt conveyors 46 projecting from the outer peripheral surface of the belt 46c of the conveyor 46 at predetermined intervals. Schema 47 and the conveyor 46
And a guide plate 48 that is inclined at the same angle as above and extends from substantially the center of the oil and fat separation tank 16 to above the oil and fat recovery tank 44 (FIG. 1). The belt conveyor 46 is provided above the oil / fat recovery tank 16 and driven by a motor with a reduction gear (not shown), and a driven pulley 46b provided to be in contact with the surface of the electrolyte 13 of the oil / fat separation tank 16. And an endless belt 46c stretched over these pulleys 46a and 46b.
Consists of

【0019】電解槽18には陽極51及び陰極52が所
定の間隔をあけかつ交互に配設され、陽極51及び陰極
52はこの実施の形態では板状に形成される(図1及び
図4)。隣接する陽極51及び陰極52間には電気絶縁
性の間隔保持具(図示せず)が介装され、この間隔保持
具により隣接する陽極51及び陰極52が接触せず上記
所定の間隔が保持されるように構成される。陽極51及
び陰極52は、グラファイト、導電性フェライト、プラ
チナ、金、チタン、カーボン、ステンレススチール、カ
ドミウム、銅、亜鉛、アルミニウム、これらの金属の合
金、金薄膜が表面に形成されたチタン、不溶性金属であ
る白金薄膜が表面に形成されたチタン、グラファイト薄
膜が表面に形成されたチタン、カドミウムが表面に形成
された銅等により形成される。更に浸漬槽14、洗浄槽
19、油脂分離槽16及び電解槽18はガラス、塩化ビ
ニール樹脂、ポリスチロール樹脂、ポリエチレン樹脂、
FRP又はアクリル樹脂によりそれぞれ形成される。
In the electrolytic cell 18, anodes 51 and cathodes 52 are alternately arranged at predetermined intervals, and the anodes 51 and the cathodes 52 are formed in a plate shape in this embodiment (FIGS. 1 and 4). . An electrically insulating spacer (not shown) is interposed between the adjacent anode 51 and cathode 52, and the predetermined distance is maintained without contact between the adjacent anode 51 and cathode 52 by the spacer. It is configured to be. The anode 51 and the cathode 52 are made of graphite, conductive ferrite, platinum, gold, titanium, carbon, stainless steel, cadmium, copper, zinc, aluminum, alloys of these metals, titanium having a gold thin film formed on the surface, insoluble metal. Is formed of titanium having a platinum thin film formed on its surface, titanium having a graphite thin film formed on its surface, copper having cadmium formed on its surface, or the like. Further, the immersion tank 14, the washing tank 19, the oil / fat separation tank 16 and the electrolytic tank 18 are made of glass, vinyl chloride resin, polystyrene resin, polyethylene resin,
Each is formed of FRP or acrylic resin.

【0020】陽極51は直流電源53のプラス端子に接
続され、陰極52はマイナス端子に接続される(図
1)。この直流電源53により陽極51及び陰極52間
に所定の電圧が印加され、電解液13中に溶出した重金
属の陽イオンを陰極52に析出させるように構成され
る。陽極51及び陰極52間には−V1の電圧が印加さ
れる、即ち図6(a)に示すように陽極51が接地さ
れ、かつ陰極52に−V1の直流電圧が印加される。V1
は1.5〜28V、更に1.5〜12Vに設定されるこ
とが好ましく、このときの電流は200〜20000
A、更に1000〜2000Aに設定されることが好ま
しい。この電流は生体11f内の重金属の含有量及び生
体11fの処理量により適宜変えられる。また2000
Aを越える電流を流すと、電解液13の温度が上昇し生
体11fが煮えてしまうおそれがある。電解槽18の底
部に陽極51及び陰極52に超音波振動を与える電極洗
浄用振動子54が設けられる。この振動子54は上記浸
透用振動子32と略同一に構成され、上記と同様に超音
波用電源38に接続される(図5)。この振動子54に
より電解槽18内の電解液13を介して陽極51及び陰
極52に所定の周波数及び所定の振幅で超音波振動が与
えられ、陽極51及び陰極52の表面に付着した油脂1
2や陰極52の表面に付着した水素の気泡(図示せず)
を離脱させるように構成される。
The anode 51 is connected to a positive terminal of a DC power supply 53, and the cathode 52 is connected to a negative terminal (FIG. 1). A predetermined voltage is applied between the anode 51 and the cathode 52 by the DC power supply 53, and the heavy metal cations eluted in the electrolyte 13 are deposited on the cathode 52. Between the anode 51 and cathode 52 voltage -V 1 is applied, ie FIGS. 6 (a) is an anode 51 as shown in the ground, and a DC voltage of -V 1 is applied to the cathode 52. V 1
Is preferably set to 1.5 to 28 V, more preferably 1.5 to 12 V, and the current at this time is 200 to 20,000.
A, and more preferably 1000 to 2000A. This current can be appropriately changed depending on the heavy metal content in the living body 11f and the processing amount of the living body 11f. Also 2000
When a current exceeding A flows, the temperature of the electrolytic solution 13 rises and the living body 11f may be boiled. An electrode cleaning vibrator 54 for applying ultrasonic vibration to the anode 51 and the cathode 52 is provided at the bottom of the electrolytic cell 18. The vibrator 54 has substantially the same configuration as the penetrating vibrator 32, and is connected to the ultrasonic power supply 38 in the same manner as described above (FIG. 5). The vibrator 54 applies ultrasonic vibration to the anode 51 and the cathode 52 at a predetermined frequency and a predetermined amplitude via the electrolytic solution 13 in the electrolytic cell 18, so that the oil and fat 1 adhering to the surfaces of the anode 51 and the cathode 52 are removed.
2 and hydrogen bubbles attached to the surface of the cathode 52 (not shown)
Is configured to be disengaged.

【0021】浸漬槽14と油脂分離槽16と電解槽18
とは循環手段56により連通接続される(図1)。これ
らの槽14,16,18の上部側面には電解液13の液
出口14d,16b,18bがそれぞれ形成され、下部
側面には電解液13の液入口14c,16a,18aが
それぞれ形成される。浸漬槽14の液出口14dは第1
オーバフローパイプ57aを介して第1ポンプ58aの
吸入口に接続され、第1ポンプ58aの吐出口は第1供
給パイプ59aを介して油脂分離槽16の液入口16a
に接続される。また油脂分離槽16の液出口16bは第
2オーバフローパイプ57bを介して第2ポンプ58b
の吸入口に接続され、第2ポンプ58bの吐出口は第2
供給パイプ59bを介して電解槽18の液入口18aに
接続される。更に電解槽18の液出口18bは第3オー
バフローパイプ57cを介して第3ポンプ58cの吸入
口に接続され、第3ポンプ58cの吐出口は第3供給パ
イプ59cを介して浸漬槽14の液入口14cに接続さ
れる。上記第1〜第3ポンプ58a〜58cは図示しな
い電動機により駆動される。浸漬槽14に貯留された電
解液13は循環手段56の第1ポンプ58aにより油脂
分離槽16に送出され、油脂分離槽16に貯留された電
解液13は第2ポンプ58bにより電解槽18に送出さ
れ、更に電解槽18に貯留された電解液13は第3ポン
プ58cにより浸漬槽14に戻されるように構成され
る。図1及び図2の符号60は浸漬槽14、油脂分離槽
16、電解槽18及び洗浄槽19の上方に設けられ電解
液13から蒸発したガスを受けるフードであり、符号6
0aは上記ガスを排出するダクトである。
An immersion tank 14, an oil / fat separation tank 16, and an electrolytic tank 18
Are connected to each other by the circulation means 56 (FIG. 1). Liquid outlets 14d, 16b, 18b of the electrolytic solution 13 are formed on upper side surfaces of these tanks 14, 16, 18 respectively, and liquid inlets 14c, 16a, 18a of the electrolytic solution 13 are formed on lower side surfaces, respectively. The liquid outlet 14d of the immersion tank 14 is the first
The outlet of the first pump 58a is connected to the suction port of the first pump 58a via an overflow pipe 57a, and the liquid inlet 16a of the oil and fat separation tank 16 is connected to the discharge port of the first oil pump 58a via a first supply pipe 59a.
Connected to. The liquid outlet 16b of the oil / fat separation tank 16 is connected to a second pump 58b through a second overflow pipe 57b.
Of the second pump 58b is connected to the suction port of the second pump 58b.
It is connected to the liquid inlet 18a of the electrolytic cell 18 via the supply pipe 59b. Further, a liquid outlet 18b of the electrolytic cell 18 is connected to a suction port of a third pump 58c via a third overflow pipe 57c, and a discharge port of the third pump 58c is connected to a liquid inlet of the immersion tank 14 via a third supply pipe 59c. 14c. The first to third pumps 58a to 58c are driven by an electric motor (not shown). The electrolyte 13 stored in the immersion tank 14 is sent to the oil / fat separation tank 16 by the first pump 58a of the circulating means 56, and the electrolyte 13 stored in the oil / fat separation tank 16 is sent to the electrolyte 18 by the second pump 58b. The electrolytic solution 13 stored in the electrolytic cell 18 is returned to the immersion tank 14 by the third pump 58c. Reference numeral 60 in FIGS. 1 and 2 denotes a hood provided above the immersion tank 14, the oil / fat separation tank 16, the electrolytic tank 18 and the cleaning tank 19 for receiving gas evaporated from the electrolytic solution 13.
0a is a duct for discharging the gas.

【0022】なお、この実施の形態では、バケットに重
金属を含む生体を収容したが、バケットに生体内に重金
属を含む生物体自体を収容してもよい。また、この実施
の形態では、搬送手段としてリフト式コンベヤを挙げた
が、ローラコンベヤ、ベルトコンベヤ又はその他の搬送
手段を用いてもよい。また、この実施の形態では、磁歪
型又はπ型の振動子を挙げたが、圧電セラミック等の電
歪型の振動子を用いてもよい。また、この実施の形態で
は、振動子にエキスポーネンシャルホーンを貼着した
が、コニカルホーン又はその他のホーンを貼着してもよ
く、これらのホーンを貼着せずに振動子を直接振動板に
貼着してもよい。また振動板を用いずに振動子を浸漬槽
等の底壁下面に上記ホーンを介して或いは直接貼着して
もよい。更に、陽極及び陰極間には図6(b)又は
(c)に示すように電圧を印加してもよい。図6(b)
に示す場合は、陽極に+V2のバイアス電圧が印加さ
れ、かつ陰極に−V1の直流電圧が印加される。図6
(c)に示す場合は、陽極に0〜+V2のバイアス電圧
が印加され、かつ陰極に0〜−V1の電圧が印加され、
これらの電圧の繰返し周波数は5〜1000Hzに設定
されることが好ましい。上記V2は0〜1.5V、V1
1.5〜28Vの範囲に設定されることが好ましい。
In this embodiment, the bucket contains the living body containing heavy metal, but the bucket may contain the living body itself containing heavy metal in the living body. Further, in this embodiment, a lift-type conveyor has been described as the conveying means, but a roller conveyor, a belt conveyor, or other conveying means may be used. In this embodiment, a magnetostrictive or π-type vibrator has been described, but an electrostrictive vibrator such as a piezoelectric ceramic may be used. Further, in this embodiment, the exponential horn is adhered to the vibrator, but a conical horn or other horn may be adhered, and the vibrator is directly adhered to the vibrator without attaching these horns. It may be stuck on. Further, the vibrator may be attached to the lower surface of the bottom wall of the immersion tank or the like via the horn or directly without using the vibrating plate. Further, a voltage may be applied between the anode and the cathode as shown in FIG. 6B or 6C. FIG. 6 (b)
If shown, the bias voltage of the anode + V 2 is applied, and a DC voltage of -V 1 is applied to the cathode. FIG.
If (c), the bias voltage of 0 to + V 2 is applied to the anode, and a voltage of 0 to-V 1 is applied to the cathode,
The repetition frequency of these voltages is preferably set to 5 to 1000 Hz. Said V 2 is 0 to 1.5 V, V 1 are preferably set in a range of 1.5~28V.

【0023】このように構成された重金属の除去装置の
動作を説明する。予め浸漬槽14、油脂分離槽16及び
電解槽18に電解液13を貯留し、循環手段56の第1
〜第3ポンプ58a〜58cを作動して上記電解液13
を循環させ、搬送手段26を所定の速度で作動させてお
く。この状態で生物体11(図3)から取出された生体
11f(図1〜図3)をバケット25に収容し、このバ
ケット25を搬送手段26のフック29に吊下げる(図
1及び図2)。このバケット25は搬送手段26により
搬送され、浸漬槽14のバケット入口14aで徐々に下
降してバケット25内の生体11fは浸漬槽14の電解
液13に浸漬される。このときバケット25内の生体1
1fには浸透用振動子32により超音波振動が与えら
れ、またバケット25は生体11fとともに所定の速度
で電解液13中を移動するので、電解液13が生体11
fに速やかに浸透し、生体11f内に含まれる重金属が
陽イオンとなって速やかに電解液13に溶出し、更に生
体11f内の油脂12が生体11fから離脱して電解液
13に分散する。このように浸透用振動子32を用いる
ことにより、電解液13の濃度を極めて薄くできるの
で、生体11fの洗浄時間を短縮できる。。
The operation of the thus configured heavy metal removing apparatus will be described. The electrolyte 13 is previously stored in the immersion tank 14, the oil / fat separation tank 16 and the electrolytic tank 18, and the first
To operate the third pumps 58a to 58c to
Is circulated, and the transport means 26 is operated at a predetermined speed. In this state, the living body 11f (FIGS. 1 to 3) taken out of the living body 11 (FIG. 3) is housed in a bucket 25, and the bucket 25 is hung on a hook 29 of a transport means 26 (FIGS. 1 and 2). . The bucket 25 is transported by the transport means 26 and gradually descends at the bucket entrance 14 a of the immersion tank 14, and the living body 11 f in the bucket 25 is immersed in the electrolyte 13 in the immersion tank 14. At this time, the living body 1 in the bucket 25
Ultrasonic vibration is given to 1f by the vibrating oscillator 32, and the bucket 25 moves in the electrolyte 13 at a predetermined speed together with the living body 11f.
f, the heavy metal contained in the living body 11f becomes a cation and elutes quickly into the electrolyte 13, and the fats and oils 12 in the living body 11f are separated from the living body 11f and dispersed in the electrolyte 13. By using the penetrating vibrator 32 in this manner, the concentration of the electrolytic solution 13 can be made extremely low, so that the cleaning time of the living body 11f can be reduced. .

【0024】浸漬槽14の電解液13は第1ポンプ58
aにより第1オーバフローパイプ57a及び第1供給パ
イプ59aを介して油脂分離槽16に送出される。油脂
分離槽16内の電解液13には油脂凝集用振動子42の
発生した超音波振動が反射板43により効率良く与えら
れるので、電解液13中に分散した油脂12は凝集して
電解液13面に速やかに浮上する。電解液13面に浮上
した油脂12はスキーマ47により掻き取られ、ガイド
板48上を通って油脂回収槽44に回収される。油脂1
2が除去された電解液13は第2ポンプ58bにより第
2オーバフローパイプ57b及び第2供給パイプ59b
を介して電解槽18に送出される。この電解液13は下
部から電解槽18に流入し、この電解液13には上昇流
が発生するので、陽極51及び陰極52間に所定の電圧
を印加すると、電解液13が電解槽18中を上昇しなが
ら電解液13中の陽イオンが陰極52に析出する。この
結果、電解槽18の底の電解液13に含まれる陽イオン
濃度が最も高く、電解槽18を上昇するに従って陽イオ
ン濃度が低くなり、陽イオン濃度の低くなった電解液1
3が電解槽18の上部の液出口18bから排出される。
この排出された電解液13は第3ポンプ58cにより第
3オーバフローパイプ57c及び第3供給パイプ59c
を介して浸漬槽14に戻される。
The electrolyte 13 in the immersion tank 14 is supplied to a first pump 58
a, it is sent to the oil / fat separation tank 16 via the first overflow pipe 57a and the first supply pipe 59a. The ultrasonic vibration generated by the vibrator 42 for aggregating fats and oils is efficiently applied to the electrolyte 13 in the fat / oil separation tank 16 by the reflection plate 43. Surface quickly on the surface. The oil 12 floating on the surface of the electrolyte 13 is scraped off by the schema 47, passes over the guide plate 48, and is collected in the oil recovery tank 44. Fats and oils 1
The electrolyte 13 from which 2 has been removed is supplied to the second overflow pipe 57b and the second supply pipe 59b by the second pump 58b.
To the electrolytic cell 18 via the The electrolytic solution 13 flows into the electrolytic cell 18 from below, and an upward flow is generated in the electrolytic solution 13. Therefore, when a predetermined voltage is applied between the anode 51 and the cathode 52, the electrolytic solution 13 flows through the electrolytic cell 18. The cations in the electrolyte 13 are deposited on the cathode 52 while rising. As a result, the cation concentration contained in the electrolytic solution 13 at the bottom of the electrolytic cell 18 is the highest, and the cation concentration decreases as the electrolytic cell 18 is raised.
3 is discharged from the liquid outlet 18b above the electrolytic cell 18.
The discharged electrolyte 13 is supplied to a third overflow pipe 57c and a third supply pipe 59c by a third pump 58c.
Is returned to the immersion tank 14 via

【0025】また電解槽18中の電解液13には僅かに
油脂12が分散している場合があり、この油脂12が陽
極51及び陰極52表面に付着する場合がある。また陰
極52表面には水素の気泡が付着する場合がある。しか
し電極洗浄用振動子54により陽極51及び陰極52に
超音波振動が与えられるので、上記油脂12や水素の気
泡が速やかに陽極51及び陰極52から離脱し、陽極5
1及び陰極52の表面は常に清浄な状態に保たれる。こ
の結果、電解液13を流れる電流密度の低下を防止でき
るので、重金属の陽イオンの陰極52への析出効率が低
下することはない。
In some cases, the fat 12 is slightly dispersed in the electrolytic solution 13 in the electrolytic cell 18, and the fat 12 may adhere to the surfaces of the anode 51 and the cathode 52. In some cases, hydrogen bubbles adhere to the surface of the cathode 52. However, ultrasonic vibration is applied to the anode 51 and the cathode 52 by the electrode cleaning vibrator 54, so that the oil 12 and hydrogen bubbles are quickly separated from the anode 51 and the cathode 52, and
1 and the surface of the cathode 52 are always kept clean. As a result, a decrease in the current density flowing through the electrolytic solution 13 can be prevented, so that the efficiency of depositing cations of heavy metals on the cathode 52 does not decrease.

【0026】一方、浸漬槽14に浸漬されたバケット2
5は浸漬槽14のバケット出口14b近傍で徐々に上昇
し、第1水切り板21の上方に至る。この第1水切り板
21の上方でバケット25内の生体11fに付着した余
分な電解液13が落下して除去される。次いでバケット
25は洗浄槽19のバケット入口19a近傍で徐々に下
降し、バケット25内の生体11fは洗浄槽19の水2
3又は中和剤に浸漬される。このときバケット25内の
生体11fには生体洗浄用振動子39により超音波振動
が与えられるので、生体11f内の電解液13が速やか
に生体11f内から排出される。この結果、生体11f
の洗浄を更に短時間で行うことができる。なお、生体1
1fを洗浄した後の水23等は排水処理装置(図示せ
ず)により所定の水質基準値内になるように処理された
後に、河川等に排出される。
On the other hand, the bucket 2 immersed in the immersion tank 14
5 gradually rises near the bucket outlet 14b of the immersion tank 14 and reaches above the first draining plate 21. Excess electrolyte 13 attached to the living body 11f in the bucket 25 is dropped and removed above the first draining plate 21. Next, the bucket 25 gradually descends near the bucket inlet 19 a of the washing tank 19, and the living body 11 f in the bucket 25
3 or immersed in a neutralizing agent. At this time, since the living body 11f in the bucket 25 is subjected to ultrasonic vibration by the living body washing vibrator 39, the electrolytic solution 13 in the living body 11f is quickly discharged from the inside of the living body 11f. As a result, the living body 11f
Can be performed in a shorter time. The living body 1
The water 23 and the like after washing 1f are discharged to a river or the like after being treated by a wastewater treatment apparatus (not shown) so as to be within a predetermined water quality reference value.

【0027】洗浄槽19のバケット出口19b近傍に達
したバケット25は徐々に上昇し、第2水切り板22の
上方で生体11fから余分の水23等が除去される。こ
のバケット25がスクリューコンベヤ41の上方に到来
すると、底網25aが自動的に又は手動で開いてバケッ
ト25内の生体11fがホッパ部41aに落下する。こ
のホッパ41a内の生体11fはスクリューコンベヤ4
1にて搬送され、箱付台車(図示せず)等に収容され
る。なお、洗浄された生体11fは農産物の肥料や家畜
の飼料等として用いられる。またこの実施の形態の装置
では、生体11fからの重金属除去処理及び生体の脱脂
処理を連続的にかつ自動的に行うことができるので、大
量の生体11fを処理するのに適する。
The bucket 25 reaching the vicinity of the bucket outlet 19b of the washing tank 19 gradually rises, and excess water 23 and the like are removed from the living body 11f above the second drain plate 22. When the bucket 25 arrives above the screw conveyor 41, the bottom net 25a opens automatically or manually, and the living body 11f in the bucket 25 falls to the hopper 41a. The living body 11f in the hopper 41a is a screw conveyor 4
1 and stored in a cart with a box (not shown) or the like. The washed living body 11f is used as fertilizer for agricultural products, feed for livestock, and the like. Further, the apparatus of this embodiment can continuously and automatically perform the heavy metal removal processing from the living body 11f and the defatting processing of the living body, and thus is suitable for processing a large amount of living body 11f.

【0028】図7は本発明の第2の実施の形態を示す。
図7において図2と同一符号は同一部品を示す。この実
施の形態では、生体11fがバケット75に収容され、
バケット75がバケット昇降手段71により浸漬槽74
に挿入されかつ引上げられ、更にバケット75の浸漬槽
74への挿入時にバケット75内の生体11fが浸漬槽
74の電解液13に浸漬されるように構成される。バケ
ット75は上記第1の実施の形態のバケットと略同一に
形成され、浸漬槽74はバケット75より一回り大きく
形成される。バケット昇降手段71は第1車輪71aを
有する第1昇降レール71bと、このレール71bに沿
って昇降しかつバケット75を係止可能な第1アーム7
1cとを有する。第1アーム71cは手動又は電動によ
り第1昇降レール71bに沿って昇降するように構成さ
れる。浸漬槽74の底部には第1の実施の形態と同様に
浸透用振動子32が設けられる。
FIG. 7 shows a second embodiment of the present invention.
7, the same reference numerals as those in FIG. 2 indicate the same parts. In this embodiment, the living body 11f is stored in the bucket 75,
The bucket 75 is moved by the bucket elevating means 71 to the immersion tank 74.
The living body 11f in the bucket 75 is immersed in the electrolyte 13 of the immersion tank 74 when the bucket 75 is inserted into the immersion tank 74. The bucket 75 is formed substantially the same as the bucket of the first embodiment, and the immersion tank 74 is formed slightly larger than the bucket 75. The bucket elevating means 71 includes a first elevating rail 71b having a first wheel 71a, and a first arm 7 which can move up and down along the rail 71b and can lock the bucket 75.
1c. The first arm 71c is configured to move up and down along the first elevating rail 71b manually or electrically. The penetrating vibrator 32 is provided at the bottom of the immersion tank 74 as in the first embodiment.

【0029】また浸漬槽74には撹拌機73が挿入さ
れ、この撹拌機73は撹拌機昇降手段72により浸漬槽
74に挿入されかつ引上げられるように構成される。撹
拌機昇降手段72は上記バケット昇降手段71と略同様
に構成され、第2車輪72aを有する第2昇降レール7
2bと、このレール72bに沿って昇降しかつ先端に撹
拌機73が固定される第2アーム72cとを有する。更
に浸漬槽74は図示しないが第1の実施の形態と同様
に、循環手段により油脂分離槽及び電解槽に連通接続さ
れ、浸漬槽で重金属除去処理及び脱脂処理された生体1
1fは図示しないが第1の実施の形態と同様の洗浄槽又
はこの実施の形態の浸漬槽と略同一の形状の洗浄槽に浸
漬されて洗浄されるように構成される。
A stirrer 73 is inserted into the immersion tank 74, and the stirrer 73 is configured to be inserted into the immersion tank 74 by the stirrer elevating means 72 and pulled up. The stirrer elevating means 72 is configured substantially in the same manner as the bucket elevating means 71, and includes a second elevating rail 7 having a second wheel 72a.
2b and a second arm 72c that moves up and down along the rail 72b and has a stirrer 73 fixed at the tip. Further, although not shown, the immersion tank 74 is connected to the oil / fat separation tank and the electrolytic tank by a circulating means in the same manner as in the first embodiment, and the living body 1 subjected to the heavy metal removal treatment and the degreasing treatment in the immersion tank.
Although not shown, 1f is configured to be immersed and cleaned in the same cleaning tank as in the first embodiment or a cleaning tank having substantially the same shape as the immersion tank of this embodiment.

【0030】このように構成された重金属の除去装置の
動作を説明する。先ず生体11fを収容したバケット7
5をバケット昇降手段71の第1アーム71cに係止し
た状態で、昇降手段71を浸漬槽74近傍まで搬送し、
第1アーム74cをバケット75ともに所定の高さまで
上昇させる。この昇降手段71を更に浸漬槽74に近付
けてバケット75を浸漬槽74の上方に位置させ、第1
アーム71cを下降させると、バケット75が生体11
fとともに浸漬槽74の電解液13に浸漬される。次い
で撹拌機昇降手段72を浸漬槽74近傍まで搬送し、第
2アーム72cを撹拌機73とともに所定の高さまで上
昇させる。この昇降手段72を更に浸漬槽74に近付け
て撹拌機73を浸漬槽74の上方に位置させ、第2アー
ム72cを下降させると、撹拌機73の羽根73aが浸
漬槽74の電解液13に浸漬される。この状態で浸透用
振動子32により生体11fに超音波振動を与えるとと
もに、撹拌機73により電解液13を撹拌する。この結
果、電解液13が生体11fに速やかに浸透し、生体1
1f内に含まれる重金属が陽イオンとなって速やかに電
解液13に溶出し、更に生体11f内の油脂が生体11
fから離脱して電解液13に分散する。
The operation of the thus configured heavy metal removing apparatus will be described. First, the bucket 7 containing the living body 11f
5 is locked to the first arm 71c of the bucket lifting / lowering means 71, and the lifting / lowering means 71 is transported to the vicinity of the immersion tank 74;
The first arm 74c is raised to a predetermined height together with the bucket 75. The raising / lowering means 71 is further moved closer to the immersion tank 74 so that the bucket 75 is positioned above the immersion tank 74.
When the arm 71c is lowered, the bucket 75
It is immersed in the electrolytic solution 13 of the immersion tank 74 together with f. Next, the stirrer elevating means 72 is conveyed to the vicinity of the immersion tank 74, and the second arm 72c is raised to a predetermined height together with the stirrer 73. When the elevating means 72 is further moved closer to the immersion tank 74 and the stirrer 73 is positioned above the immersion tank 74, and the second arm 72c is lowered, the blades 73a of the stirrer 73 are immersed in the electrolyte 13 in the immersion tank 74. Is done. In this state, ultrasonic vibration is applied to the living body 11f by the penetrating vibrator 32, and the electrolytic solution 13 is stirred by the stirrer 73. As a result, the electrolyte 13 quickly permeates the living body 11f,
Heavy metals contained in 1f become cations and are quickly eluted into the electrolyte solution 13, and oils and fats in the living body 11f
f and dispersed in the electrolyte 13.

【0031】重金属が溶出しかつ油脂が分散した電解液
13は図示しないが第1の実施の形態と同様に、油脂分
離槽に送出されて油脂が分離された後、電解槽に送出さ
れて電解液中の重金属の陽イオンが陰極に析出し、更に
浸漬槽74に戻される。所定時間経過後、撹拌機73を
浸漬槽74から引上げた後、生体11fが収容されたバ
ケット75を引上げ、このバケット75は生体11fと
ともにて洗浄槽に浸漬し、バケット75内の生体を洗浄
する。この実施の形態の装置は生体11fからの重金属
除去処理や生体11fの脱脂処理を少ない量の電解液1
3で行うことができ、少量の生体11fを処理するのに
適する。
The electrolytic solution 13 in which the heavy metals are eluted and the fats and oils are dispersed is not shown, but is sent to the fats and oils separation tank to separate the fats and oils, and then sent to the electrolysis tanks and electrolyzed as in the first embodiment. Heavy metal cations in the liquid precipitate on the cathode and are returned to the immersion tank 74. After a predetermined time has elapsed, the agitator 73 is pulled up from the immersion tank 74, and then the bucket 75 containing the living body 11f is pulled up. The bucket 75 is immersed in the washing tank together with the living body 11f to wash the living body in the bucket 75. . The apparatus according to this embodiment performs a process of removing heavy metals from the living body 11f and a degreasing treatment of the living body 11f with a small amount of the electrolyte 1.
3 and is suitable for treating a small amount of the living body 11f.

【0032】図8は本発明の第3の実施の形態を示す。
図8において図4と同一符号は同一部品を示す。この実
施の形態では、陽極81及び陰極82が丸棒状に形成さ
れ、所定の間隔をあけかつ交互に電解槽18に配設され
る。例えば陽極81が縦に3本ずつ所定の間隔をあけて
2列配設され、陰極82が上記2列の陽極81の両側及
び間に4本ずつ所定の間隔をあけて3列配設される。陽
極81及び陰極82の直径は20〜45mmの範囲に形
成されることが好ましい。陽極81は直流電源53のプ
ラス端子に接続され、陰極82はマイナス端子に接続さ
れる。また陽極81及び陰極82の材質は第1の実施の
形態の陽極及び陰極と同一である。上記以外は第1の実
施の形態と同一に構成される。このように構成された重
金属の除去装置では、陽極及び陰極の点検・交換時に全
ての陽極及び陰極を取出さなければならない上記第1の
実施の形態と比較して、この実施の形態では陽極81及
び陰極82を列毎に取出せるので、陽極81及び陰極8
2の点検・交換を容易に行うことができる。上記以外の
動作は第1の実施の形態と略同様であるので、繰返しの
説明を省略する。
FIG. 8 shows a third embodiment of the present invention.
8, the same reference numerals as those in FIG. 4 indicate the same parts. In this embodiment, the anode 81 and the cathode 82 are formed in a round bar shape, and are arranged in the electrolytic cell 18 at predetermined intervals and alternately. For example, two rows of the anodes 81 are disposed vertically at predetermined intervals, and three rows of the cathodes 82 are disposed at predetermined intervals at four sides between and on both sides of the two rows of anodes 81. . The diameters of the anode 81 and the cathode 82 are preferably formed in the range of 20 to 45 mm. The anode 81 is connected to the plus terminal of the DC power supply 53, and the cathode 82 is connected to the minus terminal. The materials of the anode 81 and the cathode 82 are the same as those of the anode and the cathode of the first embodiment. Except for the above, the configuration is the same as that of the first embodiment. In the heavy metal removing apparatus configured as described above, in this embodiment, as compared with the first embodiment in which all the anodes and the cathodes must be taken out at the time of inspection and replacement of the anodes and the cathodes, in this embodiment, the anodes 81 are removed. And the cathode 82 can be taken out for each row, so that the anode 81 and the cathode 8 can be taken out.
2 can be easily inspected and replaced. Operations other than those described above are substantially the same as those in the first embodiment, and thus, repeated description will be omitted.

【0033】図9は本発明の第4の実施の形態を示す。
この実施の形態では、電極洗浄用振動子94が電解槽の
底部ではなく、複数の陰極82の下面にそれぞれ貼着さ
れる。上記以外は第3の実施の形態と同一に構成され
る。このように構成された重金属の除去装置では、電解
槽中の電解液に僅かに分散している油脂が陰極82表面
に付着したり、或いは陰極82表面に水素の気泡が付着
したりしても、電極洗浄用振動子94により陰極82に
超音波振動が直接与えられるので、上記油脂や水素の気
泡が速やかに陰極82から離脱し、陰極82の表面は常
に清浄な状態に保たれる。この結果、電解液を流れる電
流密度の低下を防止できるので、重金属の陽イオンの陰
極82への析出効率が低下することはなく、重金属の陽
イオンを効率良く陰極82に析出させることができる。
なお、陽極表面にも油脂が付着する場合には、電極洗浄
用振動子を陰極のみならず、陽極の下面に貼着してもよ
い。これにより陽極の表面も常に清浄な状態に保つこと
ができる。
FIG. 9 shows a fourth embodiment of the present invention.
In this embodiment, the electrode cleaning vibrator 94 is attached to the lower surfaces of the plurality of cathodes 82 instead of the bottom of the electrolytic cell. Except for the above, the configuration is the same as that of the third embodiment. In the heavy metal removing apparatus configured as described above, even if fats and oils slightly dispersed in the electrolytic solution in the electrolytic cell adhere to the surface of the cathode 82 or hydrogen bubbles adhere to the surface of the cathode 82. Since the ultrasonic vibration is directly applied to the cathode 82 by the electrode cleaning vibrator 94, the bubbles of oils and fats are quickly separated from the cathode 82, and the surface of the cathode 82 is always kept in a clean state. As a result, a decrease in the current density flowing through the electrolytic solution can be prevented, so that the deposition efficiency of heavy metal cations on the cathode 82 does not decrease, and heavy metal cations can be efficiently deposited on the cathode 82.
In the case where fats and oils also adhere to the surface of the anode, the vibrator for electrode cleaning may be attached not only to the cathode but also to the lower surface of the anode. As a result, the surface of the anode can always be kept clean.

【0034】[0034]

【発明の効果】以上述べたように、本発明によれば、生
体内に重金属及び油脂が含まれる生物体又は生体と重金
属を溶解してイオン化する電解液とを浸漬槽に貯留し、
油脂分離槽の下部に電解液に超音波振動を与える油脂凝
集用振動子を設け、油脂分離槽の電解液面に浮上した油
脂を油脂排出手段が排出し、直流電源が電解槽内の陽極
及び陰極間に所定の電圧を印加して電解液中に溶出した
重金属の陽イオンを陰極に析出させ、更に循環手段が電
解槽の電解液を浸漬槽に戻すように構成したので、先ず
生体内に含まれる重金属は浸漬槽の電解液中に溶出して
陽イオンとなり、生体内に含まれる油脂は電解液に分散
し、この電解液は油脂分離槽に送出される。次に油脂凝
集用振動子により油脂分離層内の電解液に超音波振動が
与えられるので、電解液中の油脂が凝集して電解液面に
浮上した後、油脂排出手段により油脂分離槽から排出さ
れる。更に油脂が除去された電解液は電解槽に送出さ
れ、陽極及び陰極間に所定の電圧が印加されることによ
り、重金属の陽イオンが陰極に析出し、電解槽中の電解
液から上記陽イオンが除去されて浸漬槽に戻される。こ
の結果、陰極及び陽極に油脂が殆ど付着しないで、電解
液を流れる電流密度が低下せず、電解液からの重金属の
陽イオンの析出効率が低下することはない。
As described above, according to the present invention, a living body or a living body containing heavy metals and fats and oils in the living body and an electrolyte solution that dissolves and ionizes the heavy metal are stored in the immersion tank.
A grease vibrator for applying ultrasonic vibration to the electrolyte is provided at the lower part of the grease separation tank, and grease discharging means discharges grease floating on the electrolyte surface of the grease separation tank. A predetermined voltage is applied between the cathodes to deposit cations of heavy metals eluted in the electrolyte on the cathode, and furthermore, the circulation means is configured to return the electrolyte in the electrolytic tank to the immersion tank. The heavy metals contained are eluted into the electrolyte in the immersion tank to become cations, and the fats and oils contained in the living body are dispersed in the electrolyte, and this electrolyte is sent to the fat and oil separation tank. Next, ultrasonic vibration is applied to the electrolyte in the oil / fat separation layer by the vibrator for oil / fat coagulation. Is done. Further, the electrolyte from which the fats and oils have been removed is sent to the electrolytic cell, and a predetermined voltage is applied between the anode and the cathode, whereby cations of heavy metals are precipitated on the cathode, and the cations from the electrolytic solution in the electrolytic cell are removed from the electrolyte. Is removed and returned to the immersion tank. As a result, the fat and oil hardly adhere to the cathode and the anode, the current density flowing through the electrolytic solution does not decrease, and the efficiency of depositing heavy metal cations from the electrolytic solution does not decrease.

【0035】また浸漬槽の底部に生物体等に超音波振動
を与える浸透用振動子を設ければ、浸透用振動子により
発生する超音波振動により、電解液が生物体又は生体に
速やかに浸透し、生体内に含まれる重金属が陽イオンと
なって速やかに電解液に溶出し、更に生体内に含まれる
油脂が生物体等から離脱して電解液に分散する。この結
果、生物体等内の重金属の電解液への溶出速度を高める
ことができるとともに、生物体等の脱脂を速やかに行う
ことができる。また電解槽の底部又は陰極の下面に陰極
に超音波振動を与える電極洗浄用振動子を設ければ、陽
極及び陰極又は陰極の表面を常に清浄な状態に保つこと
ができ、電解液を流れる電流密度の低下を防止できるの
で、重金属の陽イオンの陰極への析出効率は低下しな
い。
If a penetrating vibrator for applying ultrasonic vibration to a living body or the like is provided at the bottom of the immersion tank, the electrolytic solution quickly penetrates the living body or living body by the ultrasonic vibration generated by the penetrating vibrator. Then, the heavy metals contained in the living body become cations and are quickly eluted into the electrolytic solution, and the fats and oils contained in the living body are separated from the living body or the like and dispersed in the electrolytic solution. As a result, the rate of elution of the heavy metal in the living body or the like into the electrolytic solution can be increased, and the living body or the like can be quickly degreased. In addition, if an electrode cleaning vibrator that applies ultrasonic vibration to the cathode is provided on the bottom of the electrolytic cell or on the lower surface of the cathode, the surface of the anode and the cathode or the cathode can always be kept clean, and the current flowing through the electrolytic solution can be maintained. Since the decrease in density can be prevented, the efficiency of depositing cations of heavy metals on the cathode does not decrease.

【0036】また浸漬槽を生物体等の搬送方向に沿って
延びて形成し、生物体等が収容されたバケットを搬送手
段が生物体等の搬送方向に搬送し、更にバケットの搬送
時にバケット内の生物体等を浸漬槽の電解液に浸漬する
ように構成すれば、生物体等からの重金属除去処理や生
物体等の脱脂処理を連続的にかつ自動的に行うことがで
きるので、大量の生物体等を処理する場合に適する。更
に生物体等が収容されたバケットをバケット昇降手段が
浸漬槽に挿入しかつ引上げ、バケットの浸漬槽への挿入
時にバケット内の生物体等を浸漬槽の電解液に浸漬する
ように構成すれば、生物体等からの重金属除去処理や生
物体等の脱脂処理を少ない量の電解液で行うことがで
き、少量の生物体等を処理する場合に適する。
Further, the immersion tank is formed so as to extend along the direction of transporting the organisms, and the transport means transports the bucket containing the organisms in the transport direction of the organisms. By immersing the living organisms in the electrolytic solution in the immersion tank, it is possible to continuously and automatically perform the heavy metal removal processing from the living organisms and the degreasing treatment of the living organisms, so that a large amount of Suitable for treating living organisms. Further, if the bucket containing the organisms is inserted into the immersion tank by the bucket elevating means and pulled up, and the organisms in the bucket are immersed in the electrolyte in the immersion tank when the bucket is inserted into the immersion tank. In addition, the treatment for removing heavy metals from living organisms and the like and the degreasing treatment for living organisms and the like can be performed with a small amount of electrolytic solution, which is suitable for treating a small amount of living organisms and the like.

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

【図1】本発明第1実施形態の生物体に含まれる重金属
の除去装置を示す断面構成図。
FIG. 1 is a cross-sectional configuration diagram showing an apparatus for removing heavy metals contained in a living organism according to a first embodiment of the present invention.

【図2】図1のA−A線断面図。FIG. 2 is a sectional view taken along line AA of FIG.

【図3】生体内に重金属が含まれるホタテガイの解剖
図。
FIG. 3 is an anatomical view of a scallop containing a heavy metal in a living body.

【図4】図1のB−B線断面図。FIG. 4 is a sectional view taken along line BB of FIG. 1;

【図5】油脂凝集用振動子、浸透用振動子及び電極洗浄
用振動子と、これらの振動子を超音波振動させる超音波
用電源とを示す構成図。
FIG. 5 is a configuration diagram showing a vibrator for oil / fat coagulation, a vibrator for permeation, and a vibrator for electrode cleaning, and an ultrasonic power supply for ultrasonically vibrating these vibrators.

【図6】陽極及び陰極間に印加される電圧を示す図。FIG. 6 is a diagram showing a voltage applied between an anode and a cathode.

【図7】本発明の第2実施形態を示す図2に対応する断
面図。
FIG. 7 is a sectional view illustrating a second embodiment of the present invention and corresponding to FIG. 2;

【図8】本発明の第3実施形態を示す図4に対応する断
面図。
FIG. 8 is a sectional view illustrating a third embodiment of the present invention and corresponding to FIG. 4;

【図9】下面に電極洗浄用振動子が貼着された陰極の要
部正面図。
FIG. 9 is a front view of a main part of a cathode having an electrode cleaning vibrator adhered to a lower surface.

【符号の説明】[Explanation of symbols]

10 重金属の除去装置 11 ホタテガイ(生物体) 11f 生体 12 油脂 13 電解液 14,74 浸漬槽 16 油脂分離槽 17 油脂排出手段 18 電解槽 25,75 バケット 26 搬送手段 32 浸透用振動子 42 油脂凝集用振動子 51,81 陽極 52,82 陰極 53 直流電源 54,94 電極洗浄用振動子 56 循環手段 71 バケット昇降手段 REFERENCE SIGNS LIST 10 Heavy metal removal device 11 Scallop (biological body) 11f Living body 12 Oil 13 Electrolyte 14, 74 Immersion tank 16 Oil separation tank 17 Oil discharge means 18 Electrolyte tank 25, 75 Bucket 26 Transport means 32 Oscillator 42 Oil and fat aggregation Oscillator 51, 81 Anode 52, 82 Cathode 53 DC power supply 54, 94 Electrode cleaning oscillator 56 Circulating means 71 Bucket elevating means

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平9−47257(JP,A) 特開 昭48−94254(JP,A) 特開 平7−8941(JP,A) 特開 昭62−38286(JP,A) 実開 昭57−51691(JP,U) (58)調査した分野(Int.Cl.6,DB名) C02F 1/461 C02F 1/36 A23L 1/33 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-9-47257 (JP, A) JP-A-48-94254 (JP, A) JP-A-7-8941 (JP, A) JP-A 62-94 38286 (JP, A) Japanese Utility Model Showa 57-51691 (JP, U) (58) Fields investigated (Int. Cl. 6 , DB name) C02F 1/461 C02F 1/36 A23L 1/33

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 生体(11f)内に重金属及び油脂(12)が含
まれる生物体(11)又は前記生体(11f)と前記重金属を溶
解してイオン化する硫酸溶液、塩酸溶液、水酸化ナトリ
ウム溶液又は塩化ナトリウム溶液からなる電解液(13)と
が貯留された浸漬槽(14,74)と、 前記浸漬槽(14,74)から送出された電解液(13)が貯留さ
れかつ前記生物体(11)又は前記生体(11f)から離脱して
分散する油脂(12)を含む前記電解液(13)に超音波振動を
与える油脂凝集用振動子(42)が底部に設けられた油脂分
離槽(16)と、 前記油脂分離槽(16)の上部に設けられ前記油脂凝集用振
動子(42)により前記電解液(13)面に浮上した油脂(12)を
前記油脂分離槽(16)から排出する油脂排出手段(17)と、 前記油脂分離槽(16)から送出された電解液(13)が貯留さ
れかつ陽極(51,81)及び陰極(52,82)が所定の間隔をあけ
て配設された電解槽(14,74)と、 前記陽極(51,81)及び前記陰極(52,82)に電気的に接続さ
れ前記陽極(51,81)及び陰極(52,82)間に所定の電圧を印
加して前記電解液(13)中に溶出した重金属の陽イオンを
前記陰極(52,82)に析出させる直流電源(53)と、 前記浸漬槽(14,74)の電解液(13)を前記油脂分離槽(16)
を介して前記電解槽(18)に送出し前記電解槽(18)の電解
液(13)を前記浸漬槽(14,74)に戻す循環手段(56)とを備
えた生物体に含まれる重金属の除去装置。
An organism (11) containing a heavy metal and a fat or oil (12) in a living body (11f) or a sulfuric acid solution, a hydrochloric acid solution, and a sodium hydroxide solution that dissolve and ionize the living body (11f) and the heavy metal. Or an immersion tank (14, 74) in which an electrolyte (13) composed of a sodium chloride solution is stored, and the electrolyte (13) sent out from the immersion tank (14, 74) is stored and the organism ( 11) or a fat separating tank provided with a fat aggregating vibrator (42) for applying ultrasonic vibration to the electrolytic solution (13) containing the fat (12) detached and dispersed from the living body (11f) is provided at the bottom ( 16), and the fat (12) floated on the electrolyte (13) surface by the fat / oil aggregating vibrator (42) provided at the upper part of the fat / oil separation tank (16) is discharged from the fat / oil separation tank (16). And an electrolyte (13) sent out from the oil / fat separation tank (16), and the anodes (51, 81) and the cathodes (52, 82) are arranged at predetermined intervals. Established electrolysis A predetermined voltage is applied between the anode (51, 81) and the cathode (52, 82) which is electrically connected to the tank (14, 74) and the anode (51, 81) and the cathode (52, 82). A direct current power source (53) for depositing cations of heavy metals eluted in the electrolyte solution (13) on the cathodes (52, 82), and the electrolyte solution (13) in the immersion tank (14, 74). Oil separation tank (16)
Circulating means (56) which sends out the electrolytic solution (13) of the electrolytic cell (18) to the immersion tank (14, 74) by sending it to the electrolytic cell (18) through Removal equipment.
【請求項2】 浸漬槽(14,74)の底部に生物体(11)又は
生体(11f)に超音波振動を与える浸透用振動子(32)が設
けられた請求項1記載の生物体に含まれる重金属の除去
装置。
2. The living organism according to claim 1, further comprising an osmotic vibrator for applying ultrasonic vibration to the living organism (11) or the living organism (11f) at the bottom of the immersion tank (14, 74). Heavy metal removal equipment included.
【請求項3】 電解槽(18)の底部又は陰極(82)の下面に
前記陰極(52,82)に超音波振動を与える電極洗浄用振動
子(54,94)が設けられた請求項1又は2記載の生物体に
含まれる重金属の除去装置。
3. An electrode cleaning vibrator (54, 94) for applying ultrasonic vibration to said cathode (52, 82) is provided on the bottom of the electrolytic cell (18) or on the lower surface of the cathode (82). Or an apparatus for removing heavy metals contained in a living organism according to 2.
【請求項4】 浸漬槽(14)が生物体(11)又は生体(11f)
の搬送方向に沿って延びて形成され、 前記生物体(11)又は前記生体(11f)が複数のバケット(2
5)に収容され、 前記複数のバケット(25)が搬送手段(26)により所定の間
隔をあけて前記生物体(11)又は前記生体(11f)の搬送方
向に沿って搬送され、 前記複数のバケット(25)の搬送時に前記複数のバケット
(25)内の生物体(11)又は生体(11f)が前記浸漬槽(14)の
電解液(13)に浸漬されるように構成された請求項1ない
し3いずれか記載の生物体に含まれる重金属の除去装
置。
4. The immersion tank (14) is a living body (11) or a living body (11f).
The living body (11) or the living body (11f) is formed so as to extend along the transport direction of the plurality of buckets (2
5), the plurality of buckets (25) are transported at predetermined intervals by transport means (26) along the transport direction of the living organism (11) or the living organism (11f), When transporting the bucket (25), the plurality of buckets
The organism (11) or the organism (11f) in (25) is included in the organism according to any one of claims 1 to 3, wherein the organism (11f) is configured to be immersed in the electrolytic solution (13) of the immersion tank (14). Heavy metal removal equipment.
【請求項5】 生物体又は生体(11f)がバケット(75)に
収容され、 前記バケット(75)がバケット昇降手段(71)により浸漬槽
(74)に挿入されかつ引上げられ、 前記バケット(75)の前記浸漬槽(74)への挿入時に前記バ
ケット(75)内の生物体又は生体(11f)が前記浸漬槽(74)
の電解液(13)に浸漬されるように構成された請求項1な
いし3いずれか記載の生物体に含まれる重金属の除去装
置。
5. An organism or living organism (11f) is stored in a bucket (75), and the bucket (75) is immersed in a dipping tank by bucket elevating means (71).
When the bucket (75) is inserted into the immersion tank (74), the organism or living body (11f) in the bucket (75) is inserted into the immersion tank (74) when the bucket (75) is inserted into the immersion tank (74).
The apparatus for removing heavy metals contained in living organisms according to any one of claims 1 to 3, wherein the apparatus is configured to be immersed in the electrolytic solution (13).
JP10257766A 1998-09-11 1998-09-11 Equipment for removing heavy metals from living organisms Expired - Fee Related JP2930947B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10257766A JP2930947B1 (en) 1998-09-11 1998-09-11 Equipment for removing heavy metals from living organisms

Publications (2)

Publication Number Publication Date
JP2930947B1 true JP2930947B1 (en) 1999-08-09
JP2000083603A JP2000083603A (en) 2000-03-28

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Country Link
JP (1) JP2930947B1 (en)

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KR100362196B1 (en) * 2000-06-30 2002-11-23 주식회사 하이닉스반도체 Apparatus for waste-water treatment in cmp process and method for the same
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