JPS5944084B2 - Metal-containing wastewater treatment equipment - Google Patents

Metal-containing wastewater treatment equipment

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Publication number
JPS5944084B2
JPS5944084B2 JP548780A JP548780A JPS5944084B2 JP S5944084 B2 JPS5944084 B2 JP S5944084B2 JP 548780 A JP548780 A JP 548780A JP 548780 A JP548780 A JP 548780A JP S5944084 B2 JPS5944084 B2 JP S5944084B2
Authority
JP
Japan
Prior art keywords
sewage
metal
supernatant
tank
settling tank
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
Application number
JP548780A
Other languages
Japanese (ja)
Other versions
JPS56102992A (en
Inventor
正春 中川
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP548780A priority Critical patent/JPS5944084B2/en
Publication of JPS56102992A publication Critical patent/JPS56102992A/en
Publication of JPS5944084B2 publication Critical patent/JPS5944084B2/en
Expired legal-status Critical Current

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  • Removal Of Specific Substances (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Description

【発明の詳細な説明】 本発明は水銀などの重金属を含む汚水を排出する前に、
汚水から重金属を有効に除去する金属含有汚水の処理装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides that, before discharging wastewater containing heavy metals such as mercury,
The present invention relates to a treatment device for metal-containing wastewater that effectively removes heavy metals from wastewater.

従来、水銀などの重金属を含む汚水を排水させる際の重
金属除去方法としては、汚水に薬剤を加えて重金属を化
合物化する方法、活性炭或はイオン交換樹脂に重金属を
吸着させる方法、及び、凝集剤によって重金属を沈殿さ
せる方法等があるが、何れの場合も、処理機能が汚水の
pH1重金属含有濃度、及び、物理的或は化学的性質に
左右され易いため、この処理に際しては繁雑な操作と温
度、pH等の管理・制御を必要とすることから、この処
理装置の設置に際しては相当の費用を必要とし、従って
、この処理装置を、例えばアマルガムを比較的小量とは
いえほぼ毎日取扱う歯科の1医院に設備することは医院
にとって相当の負担になるばかりか、現実には、汚水に
含まれる重金属は除去できてもアマルガム加工時に発生
する最も有害な水銀蒸気をも含めた状態で汚水の重金属
を処理することができないという欠点があった。
Conventional methods for removing heavy metals when draining wastewater containing heavy metals such as mercury include adding chemicals to the wastewater to convert the heavy metals into compounds, adsorbing the heavy metals on activated carbon or ion exchange resin, and using flocculants. There are methods to precipitate heavy metals, but in either case, the treatment function is easily influenced by the pH of the wastewater, the concentration of heavy metals, and its physical or chemical properties, so this treatment requires complicated operations and high temperatures. Since it requires management and control of pH, etc., installation of this processing equipment requires a considerable amount of cost. Not only does it put a considerable burden on hospitals to install such equipment in one hospital, but in reality, even if the heavy metals contained in wastewater can be removed, the heavy metals in the wastewater still contain the most harmful mercury vapor generated during amalgam processing. The disadvantage was that it could not be processed.

本発明の目的は水銀などの重金属を含む汚水から重金属
を有効に沈殿回収するとともに重金属を沈殿させた上澄
のみを排水させ、かつ、汚水発生源周囲の水銀蒸気を含
む空気をも汚水発生源から吸引除去することができる金
属含有汚水の処理装置を提供することによって、前記従
来の欠点を除去することにある。
The purpose of the present invention is to effectively precipitate and recover heavy metals from wastewater containing heavy metals such as mercury, drain only the supernatant in which the heavy metals have been precipitated, and also remove the air containing mercury vapor surrounding the wastewater source from the wastewater source. The object of the present invention is to eliminate the above-mentioned drawbacks of the conventional methods by providing a treatment device for metal-containing sewage that can be suctioned and removed from metal-containing wastewater.

次に、本発明の一実施例の構成を図面によって説明する
Next, the configuration of an embodiment of the present invention will be explained with reference to the drawings.

金属含有汚水発生源として、例えば第1図に示すヨウニ
、自在フレキシフ゛ルマウス1、バキュームチップ2、
バキュームカップ3、床掃除用アタッチメント4を備え
た1箇以上の歯科用ユニット5、及び金網製空気取入口
6上にアマルガムを載せて保存或はアマルガムを加工す
るとともに水銀蒸気吸着用活性炭フィルタ7と重金属類
の外部飛散を防止するための水8を溜めたアマルガム容
器9等とそれぞれの電磁弁10,11と配管12を介し
て連通した汚水処理装置13の密閉状本体容器14には
同容器14内を負圧にするためのブロワ15が取付けら
れ、水銀蒸気を含む容器14内エアは容器14内上部に
取付けられた活性炭フィルタ16、ブロワ15及び排気
用活性炭フィルタ17をとおって水銀蒸気が除去された
状態で大気中に排出される。
Examples of sources of metal-containing sewage include the pipe shown in Fig. 1, flexible flexible mouth 1, vacuum tip 2,
One or more dental units 5 equipped with a vacuum cup 3, a floor cleaning attachment 4, and an air intake port 6 made of wire mesh for storage or processing of the amalgam, as well as an activated carbon filter 7 for adsorbing mercury vapor. An airtight body container 14 of the sewage treatment equipment 13 is connected to an amalgam container 9 containing water 8 to prevent heavy metals from scattering to the outside, and is connected to each solenoid valve 10, 11 through a pipe 12. A blower 15 is attached to create a negative pressure inside the container 14, and the air inside the container 14 containing mercury vapor passes through an activated carbon filter 16 attached to the upper part of the inside of the container 14, a blower 15, and an activated carbon filter 17 for exhaust to remove mercury vapor. It is discharged into the atmosphere in a contaminated state.

このように形成された本体容器14内には汚水発生源か
らの金属含有汚水を配管12を介して流入させる第1沈
殿槽18が取付けられるとともに、同第1沈殿槽18内
には着脱可能な金網フィルタ19と上澄溜容器20、即
ち中空状容器の上部にエア抜ぎ孔21を形成しかつ内部
に円垂状に突出形成された底面全体に多数の小孔22を
形成した上澄溜容器20が取付けられ、配管12から流
出した汚水は、上澄溜容器20のエア抜き孔21上方に
取付けられた拡散プレート23に当たって第1沈殿槽1
8内周辺部に拡散されるとともに金網フィルタ19、上
澄溜容器20外周及び第1沈殿槽18内周をつたわって
速度を低下させた状態で自然流下し、第1沈殿槽18底
面周囲の傾斜面から第1沈殿槽18中央の窪み24に流
入するとともに、このようにして第1沈殿槽18内汚水
の水位が上昇するに従って第1沈殿槽18内汚水の上澄
は/J−fL22から浸み出るようにして上澄溜容器2
0内に流入する。
A first sedimentation tank 18 is installed in the main body container 14 formed in this way, into which metal-containing sewage from a sewage generation source flows through the pipe 12, and a removable sedimentation tank 18 is installed in the first sedimentation tank 18. A wire mesh filter 19 and a supernatant reservoir container 20, that is, a supernatant reservoir having an air release hole 21 formed in the upper part of the hollow container and a large number of small holes 22 formed throughout the bottom surface which is formed in a circular shape protruding inside. The container 20 is attached, and the sewage flowing out from the pipe 12 hits the diffusion plate 23 attached above the air vent hole 21 of the supernatant reservoir container 20 and flows into the first settling tank 1.
At the same time, it is diffused to the inner periphery of the first settling tank 18, flowing down naturally at a reduced speed through the wire mesh filter 19, the outer periphery of the supernatant tank 20, and the inner periphery of the first settling tank 18, and the slope around the bottom of the first settling tank 18. As the water level of the sewage in the first settling tank 18 rises, the supernatant of the sewage in the first settling tank 18 flows from /J-fL22 into the depression 24 at the center of the first settling tank 18. Supernatant reservoir container 2 so that it protrudes
Flows into 0.

又、第1沈殿槽18の窪み24はポンプ25、電磁弁2
6、配管27を介して密閉状第2沈殿槽28と連通し、
第1沈殿槽18内に溜った汚水は窪み24部から第2沈
殿槽28に供給されるとともに第2沈殿槽28内のエア
は排気活性炭フィルタ17をとおって大気中に排出され
、第1沈殿槽18及び第2沈殿槽28における一定水位
以上の汚水上澄はそれぞれ電磁弁29と逆止弁30、ポ
ンプ31と電磁弁32を介して排水管33から図示省略
下水道等に排水され、第2沈殿槽28底部に溜った濃縮
沈殿汚水はバルブ34を介して図示省略濾過器或はカプ
セル等に取出すことができ、又、本体容器14上部には
上澄溜容器20及び第1沈殿槽18の汚水流通部を洗い
流しながら汚水稀釈用清水を第1沈殿槽18に供給する
清水供給用配管35が取付けられ、同配管35途上には
清水制御用減圧弁36と電磁弁37が取付けられ、上澄
溜容器20の外側底面と第2沈殿槽28内には水銀の沈
殿保存用硫黄38が取付けられ、上澄溜容器20と第2
沈殿槽28には汚水の各水位に従って作動する水位検出
スイッチSWI 、SW2゜SW3が取付けられている
In addition, the depression 24 of the first settling tank 18 is connected to the pump 25 and the solenoid valve 2.
6. communicates with a sealed second settling tank 28 via piping 27;
The wastewater accumulated in the first settling tank 18 is supplied to the second settling tank 28 from the depression 24, and the air in the second settling tank 28 is discharged into the atmosphere through the exhaust activated carbon filter 17. The sewage supernatant in the tank 18 and the second settling tank 28 above a certain water level is drained from a drain pipe 33 to a sewer (not shown) etc. via a solenoid valve 29, a check valve 30, a pump 31 and a solenoid valve 32, respectively, Concentrated and settled wastewater accumulated at the bottom of the sedimentation tank 28 can be taken out to a filter or capsule (not shown) through a valve 34, and a supernatant storage container 20 and a first sedimentation tank 18 are provided at the upper part of the main body container 14. A fresh water supply piping 35 is installed to supply clean water for diluting sewage to the first settling tank 18 while flushing the sewage distribution section, and a pressure reducing valve 36 and a solenoid valve 37 for controlling fresh water are installed in the middle of the piping 35. Sulfur 38 for storing mercury precipitation is attached to the outer bottom surface of the storage container 20 and inside the second settling tank 28, and the supernatant storage container 20 and the second settling tank 28 are
The settling tank 28 is equipped with water level detection switches SWI, SW2 and SW3 which operate according to each level of wastewater.

次に、本実施例の作用を第3図の電気回路に従って説明
する。
Next, the operation of this embodiment will be explained according to the electric circuit shown in FIG.

まず、第1沈殿槽18、第2沈殿槽28の両方に汚水が
溜っていない状態において、水位検出スイッチSWI
、SW2はオフ、SW3は水位H3でオンのままの状態
にあり、この状態で、例えば朝の診療開始に従ってメイ
ンスイッチSW4をオンにすると、リレーRLIが作動
し、その常開接点RL1a1がオンしてもリレーRL2
.Rb2の常開接点RL2a1 、RL3a1がともに
オフのためリレーRL3は作動しない。
First, in a state where sewage is not accumulated in both the first settling tank 18 and the second settling tank 28, the water level detection switch SWI
, SW2 is off, and SW3 remains on at water level H3. In this state, for example, when main switch SW4 is turned on in response to the start of medical treatment in the morning, relay RLI is activated and its normally open contact RL1a1 is turned on. Even relay RL2
.. Since the normally open contacts RL2a1 and RL3a1 of Rb2 are both off, relay RL3 does not operate.

次に、この状態で診療が開始されることによる医師の手
動操作酸は機器の働きによる自動操作によって操作スイ
ッチ5W6−1 、5W6−2 、・・・・・・・・・
、5W6−nの何れかがオンすると、各スイッチSW6
に対応した歯科用ユニット50所要器具1〜4或はアマ
ルガム容器9の電磁弁10或は11が作動する他、トラ
ンスTRを介してのリレーRL4の作動によって電磁開
閉器MCが作動するとともにブロワ15駆動用モータM
が回転する。
Next, when the medical treatment is started in this state, the doctor's manual operation is automatically performed by the function of the equipment, and the operation switches 5W6-1, 5W6-2, . . .
, 5W6-n is turned on, each switch SW6
In addition to operating the solenoid valve 10 or 11 of the dental unit 50 corresponding to the required instruments 1 to 4 or the amalgam container 9, the electromagnetic switch MC is operated by the operation of the relay RL4 via the transformer TR, and the blower 15 is operated. Drive motor M
rotates.

従って、操作スイッチSW6に対応した汚水発生源周囲
のエアが配管12を介して本体容器14内に吸込まれる
とともに吸込まれたエアはエアに含まれる水銀蒸気を活
性炭フィルタ16.17に吸着させた状態で大気中に放
出され、アマルガムの加工によって重金属を含む歯科治
療時の嘲水等汚水も配管12をとおって本体容器14内
に吸込まれ、第1沈殿槽18に流入するとともに、粗大
加工屑は金網フィルタ19上に残り、金網フィルタ19
をとおった重金属含有汚水は第1沈殿槽18の窪み24
に流入する。
Therefore, the air around the sewage generation source corresponding to the operation switch SW6 is sucked into the main container 14 through the pipe 12, and the sucked air causes the mercury vapor contained in the air to be adsorbed on the activated carbon filters 16 and 17. Sewage such as water from dental treatment that is released into the atmosphere during amalgam processing and contains heavy metals is also sucked into the main container 14 through the pipe 12 and flows into the first settling tank 18, as well as coarse processing waste. remains on the wire mesh filter 19, and the wire mesh filter 19
The heavy metal-containing wastewater that has passed through is collected in the depression 24 of the first settling tank 18.
flows into.

このようにして第1沈殿槽18内汚水の水位が上昇する
とともに汚水に含まれる金属粉は第1沈殿槽18底面傾
斜面から窪み24内に徐々に沈殿して集められる他、汚
水は上澄溜容器20底面によって沈殿方向に逆う金属粉
の流入を阻止した状態でその上澄が小孔22をとおって
上澄溜容器20内に流入し、同容器20内に流入した上
澄中に含まれる金属粉は上澄溜容器20底面傾斜面から
底面外周小孔22をとおって沈殿落下して第1沈殿槽1
8の窪み24に集められるとともに、第■沈殿槽18内
汚水の水位がH1位置に達すると、水位検出スイッチS
W2がオンしてリレーRL2が作動し、H3位置でオン
のスイッチSW3とリレー接点RL1al、RL2al
を介してリレーRL3が作動する。
In this way, as the water level of the sewage in the first sedimentation tank 18 rises, the metal powder contained in the sewage gradually settles and collects from the bottom slope of the first sedimentation tank 18 into the depression 24, and the sewage is removed from the supernatant. The supernatant flows into the supernatant reservoir container 20 through the small hole 22 while the bottom surface of the reservoir container 20 prevents the metal powder from flowing in the direction of precipitation. The metal powder contained in the supernatant tank 20 is precipitated and fallen from the inclined bottom surface of the supernatant tank 20 through the small holes 22 on the outer periphery of the bottom surface, and is then deposited in the first settling tank 1.
When the wastewater is collected in the depression 24 of No. 8 and the water level in the settling tank No. 18 reaches the H1 position, the water level detection switch S is activated.
When W2 is turned on, relay RL2 is activated, and switch SW3 and relay contacts RL1al and RL2al are turned on at H3 position.
Relay RL3 is activated via.

その結果、リレー常開接点RL3a2を介してポンプ2
5と電磁弁26が作動し、第1沈殿槽18底部に溜った
金属含有濃度の高い汚水が第2沈殿槽28に流入すると
ともに、同沈殿槽28内汚水の水位がH4に達すること
による水位検出スイッチSW3のH4側オンでリレーR
L3とともにポンプ25及び電磁弁26ともオフする他
、この状態での操作スイッチSW6の作動によって第1
沈殿槽18内汚水の水位は再び上昇し、水位がH1位置
に達した時点において水位検出スイッチSW2が再びオ
ンになるが、第2沈殿槽28内汚水の水位がH4位置の
状態においては水位検出スイッチSW3がH4側に切換
えられているためリレーRL3は作動せず、第1沈殿槽
18内汚水の水位は更に上昇する。
As a result, the pump 2
5 and the electromagnetic valve 26 are activated, and the sewage with high concentration of metals accumulated at the bottom of the first settling tank 18 flows into the second settling tank 28, and the water level of the sewage in the settling tank 28 reaches H4. Relay R is turned on when H4 side of detection switch SW3 is on.
In addition to turning off the pump 25 and solenoid valve 26 together with L3, the first
The water level of the sewage in the settling tank 18 rises again, and when the water level reaches the H1 position, the water level detection switch SW2 is turned on again. Since the switch SW3 is switched to the H4 side, the relay RL3 is not activated, and the water level of the sewage in the first settling tank 18 further rises.

このようにして、第1沈殿槽18内汚水の水位がH2位
置に達して水位検出スイッチSW1がオンするとリレー
接点RL2a2.RL3b1 。
In this way, when the water level of the sewage in the first settling tank 18 reaches the H2 position and the water level detection switch SW1 is turned on, the relay contact RL2a2. RL3b1.

RL5alを介してリレーRL5が自己保持作動し、そ
の常開接点RL5a2.RL5a3を介してポンプ29
、電磁弁37、タイマTMが作動する他、診療室等に取
付けられた排水表示用パイロットランプPLが点灯し、
第1沈殿槽18内汚水の上澄は清水で稀釈された状態で
排水されるとともに清水供給は洗滌終了に対応したタイ
マアップによるタイマ接点TMb 1のオフによって停
止され、かつ、電磁弁29による上澄の排水は第1沈殿
槽18内汚水の水位がH1位置に達して水位検出スイッ
チSW2がオフになることによるリレーRL2のオフと
、その接点RL2a2を介してのリレーRL5のオフに
よって停止されるとともに、第1沈殿槽18内汚水の水
位がH2位置に達すると、再び前記排水動作が繰返され
る。
Relay RL5 is self-holding activated via RL5al, and its normally open contacts RL5a2. Pump 29 via RL5a3
, the solenoid valve 37, and the timer TM are activated, and the pilot lamp PL installed in the clinic, etc., for indicating drainage is lit.
The supernatant of the sewage in the first settling tank 18 is drained diluted with fresh water, and the supply of fresh water is stopped by turning off the timer contact TMb 1 due to the timer up corresponding to the end of washing, and Clear drainage is stopped by turning off relay RL2 when the water level of the sewage in the first settling tank 18 reaches the H1 position and turning off the water level detection switch SW2, and by turning off relay RL5 via its contact RL2a2. At the same time, when the water level of the sewage in the first settling tank 18 reaches the H2 position, the draining operation is repeated again.

このようにして1日の診療が終了した時点において、第
2沈殿槽28内汚水の重金属沈殿はほぼ完全に終了して
いるとともに、この診療終了時点においてメインスイッ
チSW4をオフにすると、リレーRL1がオフすること
によるその接点RL1b1のオンによってリレーRL6
が作動しかつその接点RL6a1を介してのポンプ31
と電磁弁32の作動によって第2沈殿槽28内汚水上澄
が排水されるとともに、第2沈殿槽28内汚水の水位が
H3位置に達することによる水位検出スイッチSW3の
H3側切換えによってリレーRL6とともにポンプ31
及び電磁弁32もオフして汚水処理装置13の全ての運
転は停止される。
At the end of the day's medical treatment in this way, the precipitation of heavy metals in the sewage in the second sedimentation tank 28 has almost completely finished, and when the main switch SW4 is turned off at the end of the medical treatment, the relay RL1 is turned off. By turning off its contact RL1b1, relay RL6 is turned on.
is activated and the pump 31 via its contact RL6a1
The sewage supernatant in the second sedimentation tank 28 is drained by the operation of the electromagnetic valve 32, and when the water level of the sewage in the second sedimentation tank 28 reaches the H3 position, the water level detection switch SW3 is switched to the H3 side, and the water level is turned off together with the relay RL6. pump 31
The solenoid valve 32 is also turned off, and all operations of the sewage treatment device 13 are stopped.

次に、朝の診療開始に従って再びメインスイッチSW4
をオンにすると、水位検出スイッチSW3がH3側に切
換っているため水位検出スイッチSW2がオンになった
時点において、はぼ完全に沈殿を終了して窪み24内に
溜った金属含有高濃度の汚水が第2沈殿槽28内に流入
するとともに、前記汚水処理装置13の運転が再び繰返
され、第2沈殿槽28内底部の汚水に含まれる金属含有
濃度は日毎に高濃度になり、この金属含有高濃度汚水は
パルプ34操作によって濾過器或はカブセル等に容易に
回収することができる。
Next, when the morning medical treatment starts, the main switch SW4 is turned on again.
When the water level detection switch SW3 is turned on, the water level detection switch SW3 is switched to the H3 side, so at the time the water level detection switch SW2 is turned on, the precipitation has almost completely finished and the high concentration metal content accumulated in the depression 24 is removed. As the sewage flows into the second settling tank 28, the operation of the sewage treatment device 13 is repeated again, and the concentration of metals contained in the sewage at the bottom of the second settling tank 28 increases day by day. The high-concentration wastewater contained therein can be easily collected into a filter, capsule, etc. by operating the pulp 34.

次に、本発明の効果について説明する。Next, the effects of the present invention will be explained.

本発明は金属含有汚水発生源に連通して同発生源からの
金属含有汚水を流入させるとともに金属含有汚水発生源
周囲の空気を負圧装置を介して吸入する第1沈殿槽と、
中空状容器の上部に空気抜き孔を形成しかつ底面に複数
筒の/ト孔を形成して第1沈殿槽内に取付けられた状態
で金属含有汚水発生源からの汚水を第1沈殿槽内周辺部
に拡散流下させるとともに第1沈殿槽内汚水の水位上昇
に従って汚水上澄を底面小孔から中空状容器内に流入さ
せる上澄溜容器と、同上澄溜容器内の汚水が予め設定し
た一定量部った状態で上澄溜容器内一定量の汚水を第1
沈殿槽内に汚水流下面をとおって供給された清水で稀釈
しながら外部に排水する第1排水装置と、第1沈殿槽底
部に溜った金属含有汚水を流水させる第2沈殿槽と、同
第2沈殿槽内金属含有汚水の沈殿作用終了に対応した時
間の経過毎に第2沈殿槽内一定量の上澄を外部に排水す
る第2排水装置とのそれぞれを備えた金属含有汚水の処
理装置にある。
The present invention includes a first settling tank that communicates with a metal-containing sewage generation source to allow metal-containing sewage from the same source to flow in, and sucks air around the metal-containing sewage source via a negative pressure device;
An air vent hole is formed in the upper part of the hollow container, and a plurality of holes are formed in the bottom surface of the hollow container. A supernatant reservoir container in which the sewage supernatant flows into the hollow container from a small hole in the bottom as the water level of the sewage in the first sedimentation tank rises, and a preset amount of sewage in the supernatant reservoir container. Pour a certain amount of wastewater into the supernatant tank with the
A first drainage device that drains water to the outside while being diluted with fresh water supplied through the lower surface of the sewage flow in the sedimentation tank; a second sedimentation tank that drains metal-containing sewage accumulated at the bottom of the first sedimentation tank; A treatment device for metal-containing sewage comprising: a second drainage device that drains a certain amount of supernatant in the second sedimentation tank to the outside at each lapse of time corresponding to the completion of the settling action of the metal-containing sewage in the second sedimentation tank; It is in.

これによって、本発明は水銀などの重金属を含・ む汚
水から重金属を有効に沈殿回収するとともに重金属を沈
殿させた上澄のみを排水させ、かつ、汚水発生源周囲の
水銀蒸気を含む空気をも汚水発生源から吸引除去するこ
とができる効果がある。
As a result, the present invention effectively precipitates and recovers heavy metals from wastewater containing heavy metals such as mercury, drains only the supernatant in which the heavy metals have been precipitated, and also removes air containing mercury vapor around the source of the wastewater. This has the effect of suctioning and removing sewage from the source.

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

第1図は本発明の一実施例の全体を示す説明図、第2図
はその要部詳細説明図、第3図はその電気回路図である
。 5・・・・・・歯科用ユニット、9・・・・・・アマル
ガム容器、10.11.26,29,32,37・・・
・・・電磁弁、12.27,35・・・・・・配管、1
3・・・・・・汚水処理装置、14・・・・・・本体容
器、15・・・・・・ブロワ、18・・・・・・第1沈
殿槽、20・・・・・・上澄溜容器、21・・・・・・
エア抜き孔、22・・・・・・小孔、25,31・・・
・・・ポンプ、28・・・・・・第2沈殿槽。
FIG. 1 is an explanatory diagram showing the whole of one embodiment of the present invention, FIG. 2 is a detailed explanatory diagram of the main part thereof, and FIG. 3 is an electric circuit diagram thereof. 5... Dental unit, 9... Amalgam container, 10.11.26, 29, 32, 37...
...Solenoid valve, 12.27,35...Piping, 1
3...Sewage treatment equipment, 14...Main container, 15...Blower, 18...First settling tank, 20...Top Clearing container, 21...
Air vent hole, 22... Small hole, 25, 31...
...Pump, 28...Second sedimentation tank.

Claims (1)

【特許請求の範囲】[Claims] 1 金属含有汚水発生源に連通して同発生源からの金属
含有汚水を流入させるとともに金属含有汚水発生源周囲
の空気を負圧装置を介して吸入する第1沈殿槽と、中空
状容器の上部に空気抜き孔を形成しかつ底面に複数筒の
/ト孔を形成して第1沈殿槽内に取付けられた状態で金
属含有汚水発生源からの汚水を第1沈殿槽内周辺部に拡
散流下させるとともに第1沈殿槽内汚水の水位上昇に従
って汚水上澄を底面小孔から中空状容器内に流入させる
上澄溜容器と、同上澄溜容器内の汚水が予め設定した=
定量溜った状態で上澄溜容器内一定量の汚水を第1沈殿
槽内に汚水流下面をとおって供給された清水で稀釈しな
がら外部に排水する第1排水装置と、第1沈殿槽底部に
溜った金属含有汚水を流入させる第2沈殿槽と、同第2
沈殿槽内金属含有汚水の沈殿作用終了に対応した時間の
経過毎に第2沈殿槽内一定量の上澄を外部に排水する第
2排水装置とのそれぞれを備えることを特徴とする金属
含有汚水の処理装置。
1. A first sedimentation tank that communicates with a metal-containing sewage source to allow metal-containing sewage from the source to flow in and sucks air around the metal-containing sewage source via a negative pressure device, and an upper part of a hollow container. An air vent hole is formed in the bottom surface, and a plurality of cylindrical holes are formed in the bottom surface, and the wastewater from the metal-containing sewage generation source is diffused and flowed down to the periphery of the first sedimentation tank while installed in the first sedimentation tank. At the same time, as the water level of the sewage in the first sedimentation tank rises, the sewage supernatant flows into the hollow container from the small hole in the bottom of the supernatant container, and the sewage in the supernatant container is set in advance.
a first drainage device that drains a certain amount of sewage in the supernatant reservoir container to the outside while diluting it with fresh water supplied through the lower surface of the sewage flow into the first settling tank; and a bottom part of the first settling tank. a second sedimentation tank into which metal-containing wastewater accumulated in the tank flows;
and a second drainage device that drains a certain amount of supernatant in the second settling tank to the outside every time corresponding to the end of the settling action of the metal-containing sewage in the settling tank. processing equipment.
JP548780A 1980-01-21 1980-01-21 Metal-containing wastewater treatment equipment Expired JPS5944084B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP548780A JPS5944084B2 (en) 1980-01-21 1980-01-21 Metal-containing wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP548780A JPS5944084B2 (en) 1980-01-21 1980-01-21 Metal-containing wastewater treatment equipment

Publications (2)

Publication Number Publication Date
JPS56102992A JPS56102992A (en) 1981-08-17
JPS5944084B2 true JPS5944084B2 (en) 1984-10-26

Family

ID=11612593

Family Applications (1)

Application Number Title Priority Date Filing Date
JP548780A Expired JPS5944084B2 (en) 1980-01-21 1980-01-21 Metal-containing wastewater treatment equipment

Country Status (1)

Country Link
JP (1) JPS5944084B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4909573B2 (en) * 2005-06-17 2012-04-04 日立オートモティブシステムズ株式会社 Rotating electric machine and manufacturing method thereof
JP4904989B2 (en) * 2006-08-24 2012-03-28 株式会社日立製作所 Rotating electrical machines, winding machines, rotating electrical machine systems, hybrid vehicles, fuel cell vehicles, and electric vehicles
CN105384218A (en) * 2015-12-16 2016-03-09 无锡吉进环保科技有限公司 New ionizing type sewage processor

Also Published As

Publication number Publication date
JPS56102992A (en) 1981-08-17

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