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JP2000262807A - Liquid separation discharge device and liquid separation discharge method - Google Patents
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JP2000262807A - Liquid separation discharge device and liquid separation discharge method - Google Patents

Liquid separation discharge device and liquid separation discharge method

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Publication number
JP2000262807A
JP2000262807A JP11078326A JP7832699A JP2000262807A JP 2000262807 A JP2000262807 A JP 2000262807A JP 11078326 A JP11078326 A JP 11078326A JP 7832699 A JP7832699 A JP 7832699A JP 2000262807 A JP2000262807 A JP 2000262807A
Authority
JP
Japan
Prior art keywords
liquid
discharge
separated
water tank
liquid level
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.)
Granted
Application number
JP11078326A
Other languages
Japanese (ja)
Other versions
JP4348766B2 (en
Inventor
Katsuaki Matsuzawa
克明 松澤
Kenichi Tawara
賢一 田原
Toshiichiro Ueno
俊一朗 上野
Junya Nishino
順也 西野
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.)
IHI Corp
Original Assignee
Ishikawajima Harima Heavy Industries Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP07832699A priority Critical patent/JP4348766B2/en
Publication of JP2000262807A publication Critical patent/JP2000262807A/en
Application granted granted Critical
Publication of JP4348766B2 publication Critical patent/JP4348766B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【課題】 上下に層分離する2種以上の液体の液レベル
を検出してそれぞれを自動的に分離排出できる新規な液
分離排出装置及び液分離排出方法の提供。 【解決手段】 互いに比重と粘度の異なる2種以上の液
体からなる混合液が流れ込む水槽1と、この水槽1内部
で層分離した上層液と下層液とをそれぞれ排出する排出
ライン2a,2b と、上記上層液の液面高さと下層液の液面
高さをそれぞれの回転子の回転数又は回転抵抗の変化に
よって検知する回転型粘度計3a,3b と、この回転型粘度
計3a,3b によって検知された各分離液の液面高さに応じ
て上記各排出ライン2a,2b のバルブ4a,4b を開閉制御す
る制御部5とを備える。
PROBLEM TO BE SOLVED: To provide a novel liquid separation / discharge device and a liquid separation / discharge method capable of detecting the liquid level of two or more kinds of liquids vertically separated and automatically separating and discharging each of them. SOLUTION: A water tank 1 into which a mixture of two or more liquids having different specific gravities and viscosities flows into each other, and discharge lines 2a and 2b for discharging an upper liquid and a lower liquid separated in the water tank 1 respectively, Rotary viscometers 3a and 3b that detect the liquid level height of the upper layer liquid and the liquid level of the lower layer liquid by changes in the number of revolutions or rotational resistance of the respective rotors, and are detected by the rotary viscometers 3a and 3b. A control unit 5 for controlling the opening and closing of the valves 4a and 4b of the discharge lines 2a and 2b in accordance with the liquid level of each of the separated liquids.

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、例えば、都市ゴミ
処理設備の乾留炉からでる水と油又は灰溶融炉のメタル
とスラグ等といった互いに比重及び粘度の異なる結果、
上下に層分離する2種以上の液体をそれぞれ分離して排
出する液分離排出装置及び液分離排出方法に関するもの
である。
BACKGROUND OF THE INVENTION The present invention relates to a method for producing water and oil from a dry distillation furnace of a municipal refuse treatment facility or a metal and slag of an ash melting furnace, which have different specific gravities and viscosities.
The present invention relates to a liquid separation / discharge device and a liquid separation / discharge method for respectively separating and discharging two or more types of liquids which are vertically separated.

【0002】[0002]

【従来の技術及び課題が解決しようとする課題】従来、
水と油等のように比重の異なる2種類以上の液体の混合
液を分離して排出する方法としては、かかる混合液を水
槽等に一時的に貯留させて上下に層分離させた後、それ
ぞれの液体層に排出口を有する排出ラインを設け、これ
ら各排出ラインからポンプ等によってそれぞれの液体を
別個に排出する方法が一般的に知られている。また、こ
のような分離排出方法においては、それぞれの液レベル
を検出するために、上下に層分離した各液体のほぼ中間
の比重を有するフロートを透明な水槽中に投入し、その
フロートの高さ位置を水槽の側面等から目視によって確
認することで各液体の液レベルを検出するようになって
いる。
2. Description of the Related Art
As a method of separating and discharging a liquid mixture of two or more types of liquids having different specific gravities, such as water and oil, the liquid mixture is temporarily stored in a water tank or the like, and separated into layers vertically, and then each is separated. A method is generally known in which a discharge line having a discharge port is provided in a liquid layer, and each liquid is separately discharged from each of the discharge lines by a pump or the like. Further, in such a separation and discharge method, in order to detect each liquid level, a float having a substantially specific gravity of each liquid vertically separated into layers is put into a transparent water tank, and the height of the float is set. The liquid level of each liquid is detected by visually checking the position from the side of the water tank or the like.

【0003】従って、従来の液分離排出方法は、このフ
ロートの高さ位置を作業員が目視してそれぞれの液体の
液レベルを確認しながら交互にあるいは、同時にそれぞ
れの液体を各排出ラインから手作業で排出することにな
る。
[0003] Therefore, in the conventional liquid separation and discharge method, an operator visually checks the height position of the float and checks the liquid level of each liquid, and manually or alternately simultaneously discharges each liquid from each discharge line. It will be discharged by work.

【0004】しかしながら、このような従来方法では、
フロートの高さ位置を外部から水槽越しに目視できるよ
うなほぼ透明に近い液体の場合にしか利用できず、フロ
ートの位置を目視できない色の濃い液体(タール等)や
水槽自体が非透明の場合には、適用することができない
といった不都合がある。また、この方法の場合は、水槽
のサイズが大型化するに従ってフロートが益々目視でき
難くなる上に、その回収も容易でないといった問題点が
ある。さらに、対象とする液体が、例えば灰溶融炉から
でるメタルとスラグといった極めて高温の液体では、こ
の温度に耐え得るフロートが見あたらない上に、作業員
が近寄ることができないため、この方法を適用すること
は不可能である。また、各液体の排出制御は作業員の労
力によるものであるため、効率が悪く、自動化が望まれ
ている。
However, in such a conventional method,
It can be used only when the liquid is almost transparent so that the height of the float can be seen from outside through the water tank, and when the float position is dark liquid (tar etc.) or the water tank itself is not transparent. Has the disadvantage that it cannot be applied. In addition, in the case of this method, there is a problem that as the size of the water tank increases, the float becomes more and more difficult to see and the recovery thereof is not easy. Further, when the target liquid is an extremely high-temperature liquid such as metal and slag coming out of an ash melting furnace, a float that can withstand this temperature is not found, and an operator cannot approach the liquid. It is impossible. In addition, since the control of the discharge of each liquid is performed by the labor of an operator, the efficiency is low and automation is desired.

【0005】そこで、本発明はこのような課題を有効に
解決するために案出されたものであり、その主な目的は
上下に層分離する2種以上の混合液体を分離して自動的
に排出できる新規な液分離排出装置及び液分離排出方法
を提供するものである。
Accordingly, the present invention has been devised in order to effectively solve such a problem, and a main object of the present invention is to separate two or more kinds of mixed liquids which are separated into upper and lower layers and to automatically separate them. It is intended to provide a novel liquid separation / discharge device and a liquid separation / discharge method capable of discharging.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
に本発明は、互いに比重と粘度の異なる2種以上の液体
からなる混合液体が流れ込む水槽と、この水槽内部で上
下に層分離した上層液と下層液とをそれぞれ排出する排
出ラインと、その水槽内に位置すると共に、上記上層液
の液面高さと下層液の液面高さをそれぞれの回転子の回
転数又は回転抵抗の変化によって検知する回転型粘度計
と、この回転型粘度計によって検知された各分離液の液
面高さに応じて上記各排出ラインのバルブを開閉制御す
る制御部とを備えたものである。そして、このような液
分離排出装置を用い、上記水槽内で層分離した上層液と
下層液の液面高さがそれぞれ各回転型粘度計の回転子に
達したときに上記各排出ラインのバルブを開いてそれぞ
れの分離液を排出し、その後、各液面が回転子のレベル
を下回ったときに上記各排出ラインのバルブを閉じて排
出を停止するようにしたものである。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a water tank into which a mixed liquid composed of two or more liquids having different specific gravities and viscosities flows, and an upper layer vertically separated inside the water tank. A discharge line for discharging the liquid and the lower liquid, respectively, and located in the water tank, and the liquid surface height of the upper liquid and the liquid surface height of the lower liquid are changed by changing the rotation speed or rotation resistance of each rotor. It comprises a rotary viscometer for detecting, and a control unit for controlling opening and closing of the valves of the respective discharge lines in accordance with the liquid level of each separated liquid detected by the rotary viscometer. Then, using such a liquid separation and discharge device, when the liquid level of the upper liquid and the lower liquid separated in the water tank reaches the rotor of each rotary viscometer, the valve of each of the discharge lines is discharged. Is opened to discharge each of the separated liquids, and thereafter, when the liquid levels fall below the level of the rotor, the valves of the respective discharge lines are closed to stop the discharge.

【0007】すなわち、本発明は上層液と下層液との比
重差のみならず、粘度差に着目し、それらの粘度差の違
いを回転型粘度計によって検出することで各液体の液レ
ベルを把握し、この回転型粘度計によって検出された各
液レベルに応じて各液体の排出ラインのバルブを開閉制
御するようにしたものである。
That is, the present invention focuses not only on the specific gravity difference between the upper liquid and the lower liquid, but also on the viscosity difference, and detects the difference in the viscosity with a rotary viscometer to grasp the liquid level of each liquid. In addition, the valve of the discharge line for each liquid is controlled to open and close according to each liquid level detected by the rotary viscometer.

【0008】これによって、従来のように透明な液体は
勿論、タール等のような色の濃い液体や溶融メタル/ス
ラグ等といった高温の液体であっても容易かつ正確にそ
の液レベルを検知し、各液体の分離排出制御を自動的に
行うことができる。
[0008] This makes it possible to easily and accurately detect the liquid level of not only a transparent liquid as in the past but also a dark liquid such as tar or a high-temperature liquid such as molten metal / slag. Separate discharge control of each liquid can be performed automatically.

【0009】[0009]

【発明の実施の形態】次に、本発明を実施する好適一形
態を添付図面を参照しながら説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, a preferred embodiment of the present invention will be described with reference to the accompanying drawings.

【0010】図1は本発明に係る液分離装置の実施の一
形態を示したものである。
FIG. 1 shows an embodiment of a liquid separating apparatus according to the present invention.

【0011】図示するように、この液分離装置は、互い
に比重と粘度の異なる2種類の液体からなる混合液体、
例えば、水と油やタール,スラグと溶融メタル等が混合
した状態で流れ込む水槽1と、この水槽1内部で層分離
した上層液と下層液とをそれぞれ排出する排出ライン2
a,2bと、これら各分離液の液面高さをそれぞれの検
出する回転型粘度計3a,3bと、これら各回転型粘度
計3a,3bによって検出された各分離液U,Lの液面
高さに応じて上記各排出ライン2a,2bのバルブ4
a,4bを開閉制御する制御部5とから主に構成されて
いる。
As shown in the figure, this liquid separating apparatus comprises a mixed liquid composed of two types of liquids having different specific gravities and different viscosities.
For example, a water tank 1 into which water and oil or tar, slag and molten metal, etc. flow, and a discharge line 2 for discharging the upper liquid and the lower liquid separated in the water tank 1 respectively.
a, 2b, rotary viscometers 3a, 3b for detecting the liquid level of each of the separated liquids, and liquid surfaces of the separated liquids U, L detected by the rotary viscometers 3a, 3b, respectively. The valve 4 of each of the discharge lines 2a and 2b according to the height
The control section 5 mainly controls the opening and closing of the switches a and 4b.

【0012】この回転型粘度計3a,3bは、それそれ
水槽1内の分離液中で回転する回転子(プロペラ)6
と、この回転子6を垂直に支持するパイプ状の支持ロッ
ド7と、この支持ロッド7を支持すると共に回転子6を
回転駆動する駆動部8とから構成されており、各分離液
の粘度の違いによる回転数又は回転抵抗の変化、すなわ
ち回転数を一定に保つべく変化するトルクを検知して各
分離液の液レベルを検出し、その液レベル検出信号を上
記制御部5にそれぞれ入力するようになっている。
The rotary viscometers 3a and 3b are each provided with a rotor (propeller) 6 which rotates in the separated liquid in the water tank 1.
And a pipe-shaped support rod 7 that vertically supports the rotor 6, and a driving unit 8 that supports the support rod 7 and drives the rotor 6 to rotate. A change in rotation speed or rotation resistance due to the difference, that is, a torque that changes to keep the rotation speed constant, is detected to detect the liquid level of each separated liquid, and the liquid level detection signal is input to the control unit 5 respectively. It has become.

【0013】また、排出ライン2a,2bは水槽1の側
面にそれぞれ上下、すなわち、排出ライン2a側が水槽
1の底部に接続されると共に、排出ライン2b側が水槽
1の中段部、より詳しくは回転型粘度計3a側の回転子
6より上方の位置にそれぞれ接続されており、上下に層
分離した各分離液をそれぞれの排出ライン2a,2bか
ら分離排出するようになっている。さらに、これら排出
ライン2a,2bに設けられたバルブ4a,4bは、例
えば、電磁バルブなどのように瞬時に応答するものから
なっており、制御部5からの制御信号によってそれぞれ
の排出ライン2a,2bを瞬時に開閉して各分離液の排
出停止を行うようになっている。
The discharge lines 2a and 2b are vertically connected to the side of the water tank 1, that is, the discharge line 2a is connected to the bottom of the water tank 1, and the discharge line 2b is connected to the middle part of the water tank 1, more specifically, the rotary type. The viscometer 3a is connected to a position above the rotor 6 on the side of the viscometer 3a, and separates the separated liquid vertically separated from the viscometer 3a through respective discharge lines 2a and 2b. Further, the valves 4a and 4b provided on the discharge lines 2a and 2b are configured to respond instantaneously, for example, such as electromagnetic valves, and the respective discharge lines 2a, 2b are controlled by a control signal from the control unit 5. 2b is opened and closed instantaneously to stop the discharge of each separated liquid.

【0014】また、図中9は上記混合液を供給するため
の供給ラインであり、供給後の混合液の分離を促進すべ
く水槽1の底部側にから水槽1内に混合液を供給するよ
うになっている。
Reference numeral 9 in the drawing denotes a supply line for supplying the above-mentioned mixed liquid, which is supplied from the bottom side of the water tank 1 into the water tank 1 to promote separation of the mixed liquid after the supply. It has become.

【0015】次に、このような構成をした液分離排出装
置を用いて本発明方法の一例を説明する。
Next, an example of the method of the present invention will be described using the liquid separating / discharging apparatus having such a configuration.

【0016】先ず、各排出ライン2a,2bの各バルブ
4a,4bを閉じると共に、各回転型粘度計3a,3b
の回転子6,6をそれぞれ回転駆動させた状態としてか
ら供給ライン9から水槽1内に、互いに比重と粘度の異
なる2種類の液体からなる混合液を連続して流し込む。
すると、この混合液がその比重の違いにより水槽1内で
上下に層分離すると共に、それらの液面が徐々に上昇し
てくる。
First, each valve 4a, 4b of each discharge line 2a, 2b is closed, and each rotary viscometer 3a, 3b
After the rotors 6 and 6 are driven to rotate, mixed liquids composed of two kinds of liquids having different specific gravities and different viscosities are continuously poured into the water tank 1 from the supply line 9.
Then, the mixed liquid is separated into layers vertically in the water tank 1 due to the difference in specific gravity, and their liquid levels gradually rise.

【0017】そして、この液面の上昇によって最初に上
層液側の液面が水槽1内下方に位置している回転型粘度
計3aの回転子6のレベルに到達することで、その回転
子6のトルクが上がることになるが、この時点では、制
御部5はその検知信号を受け取っても排出ライン2a,
2bのいずれのバルブ4a,4bを制御せずそのまま閉
じた状態としておく。
When the liquid level of the upper layer liquid first reaches the level of the rotor 6 of the rotary viscometer 3a located in the lower part of the water tank 1 by the rise of the liquid level, the rotor 6 However, at this time, the control unit 5 receives the detection signal, and the discharge line 2a,
The valves 4a and 4b of 2b are kept closed without being controlled.

【0018】次に、このようにして各分離液の液レベル
がさらに上昇して上層液の液面が上方に位置している回
転型粘度計3bの回転子6のレベルに達し、その回転子
6の回転数が上がると、図2に示すように、制御部5が
これを検知し、液レベルが上限に達したと判断して中段
部の排出ライン2bのバルブ4bを開いて排出ライン2
bから上層液の一部を排出する。これによって、上層液
の液レベルが降下すると共に、上層液のみを排出ライン
2bから水槽1外へ分離排出することができる。そし
て、この上層液の液レベルの降下に伴って回転型粘度計
3bの回転子6が液面上に露出してそのトルクが下がっ
たならば、再び、制御部5がこれを検知し、液レベルが
下がったと判断して排出ライン2bのバルブ4bを閉じ
て上層液の排出を停止する。その後、再び、上層液の液
レベルが上昇したならば、上記と同様に排出ライン2b
のバルブ4bの開閉制御を繰り返すことで上層液のみを
排出ライン2bから水槽1外へ効果的に分離排出するこ
とができる。
Next, the liquid level of each of the separated liquids further rises in this way to reach the level of the rotor 6 of the rotary viscometer 3b in which the liquid level of the upper layer liquid is located above, and the rotor As shown in FIG. 2, when the rotation speed of the motor 6 is increased, the controller 5 detects this, determines that the liquid level has reached the upper limit, opens the valve 4b of the discharge line 2b in the middle stage, and opens the discharge line 2
Part of the upper liquid is discharged from b. As a result, the liquid level of the upper layer liquid drops, and only the upper layer liquid can be separated and discharged from the discharge line 2b to the outside of the water tank 1. If the rotor 6 of the rotary viscometer 3b is exposed on the liquid surface and the torque decreases with the decrease of the liquid level of the upper layer liquid, the control unit 5 detects this again, and When it is determined that the level has dropped, the valve 4b of the discharge line 2b is closed to stop discharging the upper layer liquid. Thereafter, if the liquid level of the upper layer liquid rises again, the discharge line 2b
By repeating the opening and closing control of the valve 4b, only the upper layer liquid can be effectively separated and discharged from the discharge line 2b to the outside of the water tank 1.

【0019】一方、この上層液の上昇に伴って下層液の
液レベルも上昇し、排出ライン2b付近まで達すること
になるが、その前に下方に位置している回転型粘度計3
aの回転子6に達した時点で、この回転子6が上層液と
下層液との粘度の違いによりさらにトルクが変化するこ
とにより、そのレベルに達したことを検知することにな
る。そして、レベル信号を受けた制御部5が図3に示す
ように、排出ライン2aのバルブ4aを開いてその下層
液を排出ライン2aから排出することになるため、下層
液の液レベルの上昇が抑制されて中段の排出ライン2b
側から排出されるようなことがなくなると共に、水槽1
中から下層液のみを水槽1外へ分離排出することができ
る。その後、このようにして下層液の液レベルが降下し
て回転型粘度計3aの回転子6の回転数が上昇したなら
ば、制御部5がこれを検知し、排出ライン2aのバルブ
4aを閉じて下層液の排出を停止することになる。そし
て、その後は上層液と同様に、この下層液の液レベルに
応じて排出ライン2bのバルブ4bの開閉制御を行うこ
とによって上層液のみを排出ライン2bから水槽1外へ
分離排出することができる。
On the other hand, the liquid level of the lower layer liquid also rises with the rise of the upper layer liquid, and reaches the vicinity of the discharge line 2b.
When the rotor 6 reaches the rotor 6a, the torque of the rotor 6 further changes due to the difference in viscosity between the upper liquid and the lower liquid, thereby detecting that the rotor 6 has reached that level. Then, as shown in FIG. 3, the control unit 5 that has received the level signal opens the valve 4a of the discharge line 2a and discharges the lower layer liquid from the discharge line 2a. Suppressed middle discharge line 2b
It is no longer discharged from the side and the tank 1
Only the lower layer liquid can be separated and discharged out of the water tank 1 from the inside. Thereafter, if the liquid level of the lower layer liquid drops and the rotation speed of the rotor 6 of the rotary viscometer 3a increases, the control unit 5 detects this and closes the valve 4a of the discharge line 2a. As a result, the discharge of the lower layer liquid is stopped. Then, similarly to the upper liquid, by controlling the opening and closing of the valve 4b of the discharge line 2b according to the liquid level of the lower liquid, only the upper liquid can be separated and discharged from the discharge line 2b to the outside of the water tank 1. .

【0020】このように、本発明は上層液と下層液との
比重差のみならず、粘度差に着目し、それらの粘度差の
違いを二つの回転型粘度計によって検出して各液体の液
レベルを検出し、検出された各液体の液レベルに応じて
排出ラインのバルブを開閉制御するようにしたものであ
るため、作業員の労力に頼ることなく自動的に液分離排
出を行うことができる。しかも、その液レベルの検出を
回転型粘度計によって検出するようにしたため、従来の
ように透明な液体は勿論、タール等のような色の濃い液
体や溶融メタル/スラグ等といった高温の液体であって
も容易かつ正確にその液レベルの検知し、正確な分離排
出制御を行うことができる。
As described above, the present invention focuses not only on the difference in specific gravity between the upper liquid and the lower liquid, but also on the viscosity difference, and detects the difference in the viscosity by two rotary viscometers to detect the liquid difference of each liquid. Since the level is detected and the valve of the discharge line is controlled to open and close according to the detected liquid level, liquid separation and discharge can be performed automatically without relying on the labor of the operator. it can. In addition, since the liquid level is detected by a rotary viscometer, the liquid level is not only a transparent liquid as in the past, but also a dark liquid such as tar and a high-temperature liquid such as molten metal / slag. Even so, it is possible to easily and accurately detect the liquid level and perform accurate separation and discharge control.

【0021】尚、本実施の形態では、比重及び粘度の異
なる2種類の液体からなる混合液体を分離排出するよう
にした例で示したが、粘度及び比重の異なる3種類以上
の液体の混合液体であっても、上述した回転型粘度計及
び排出ラインをその数に応じてそれぞれ設置高さを異な
らしめて設置すれば、上記と同様にそれぞれの液体毎に
自動的かつ確実に分離排出することが可能となる。
In this embodiment, an example has been described in which a mixed liquid composed of two kinds of liquids having different specific gravities and viscosities is separated and discharged. However, a mixed liquid of three or more liquids having different viscosities and specific gravities is shown. Even if the above-mentioned rotary viscometers and discharge lines are installed with different installation heights according to the number thereof, it is possible to automatically and reliably separate and discharge each liquid in the same manner as described above. It becomes possible.

【0022】[0022]

【発明の効果】以上要するに本発明によれば、2種以上
の液体の混合液のそれぞれの液レベルの検出と分離排出
を作業員の労力に頼ることなく自動的かつ確実に行うこ
とができる。また、その液レベルの検出を回転型粘度計
によって検出するようにしたため、従来のように透明な
液体は勿論、タール等のような色の濃い液体や溶融メタ
ル/スラグ等といった高温の液体であっても容易かつ正
確にその液レベルを検知し、正確な分離排出制御を行う
ことができる等といった優れた効果を発揮することがで
きる。
In summary, according to the present invention, the detection and the separation and discharge of each liquid level of a mixture of two or more liquids can be performed automatically and reliably without relying on the labor of an operator. Since the liquid level is detected by a rotary viscometer, the liquid level is not only a transparent liquid as in the past, but also a dark liquid such as tar or a high-temperature liquid such as molten metal / slag. However, excellent effects such as easy and accurate detection of the liquid level and accurate separation / discharge control can be achieved.

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

【図1】本発明に係る液分離排出装置の実施の一形態を
示す構成図である。
FIG. 1 is a configuration diagram showing one embodiment of a liquid separation and discharge device according to the present invention.

【図2】本発明に係る液分離排出装置を用いた液分離方
法の実施の一形態を示す概念図である。
FIG. 2 is a conceptual diagram showing one embodiment of a liquid separation method using the liquid separation / discharge device according to the present invention.

【図3】本発明に係る液分離排出装置を用いた液分離方
法の実施の一形態を示す概念図である。
FIG. 3 is a conceptual diagram showing one embodiment of a liquid separation method using the liquid separation and discharge device according to the present invention.

【符号の説明】[Explanation of symbols]

1 水槽 2a,2b 排出ライン 3a,3b 回転型粘度計 4a,4b バルブ 5 制御部 6 回転子 7 支持ロッド 8 駆動部 9 供給ライン Reference Signs List 1 Water tank 2a, 2b Discharge line 3a, 3b Rotary viscometer 4a, 4b Valve 5 Control unit 6 Rotor 7 Support rod 8 Drive unit 9 Supply line

フロントページの続き (72)発明者 上野 俊一朗 神奈川県横浜市磯子区新中原町1番地 石 川島播磨重工業株式会社技術研究所内 (72)発明者 西野 順也 神奈川県横浜市磯子区新中原町1番地 石 川島播磨重工業株式会社技術研究所内 Fターム(参考) 4D051 AA01 BA07 BA09 Continued on the front page (72) Inventor Shun-ichiro Ueno 1 Shin-Nakahara-cho, Isogo-ku, Yokohama-shi, Kanagawa Pref. Ishikawajima-Harima Heavy Industries Co., Ltd. Ishikawashima Harima Heavy Industries, Ltd. Technical Research Laboratory F-term (reference) 4D051 AA01 BA07 BA09

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 互いに比重と粘度の異なる2種以上の液
体からなる混合液が流れ込む水槽と、この水槽内部で層
分離した上層液と下層液とをそれぞれ排出する排出ライ
ンと、上記上層液の液面高さと下層液の液面高さをそれ
ぞれの設置高さの異なる回転子の回転数又は回転抵抗の
変化によって検知する回転型粘度計と、この回転型粘度
計によって検知された各分離液の液面高さに応じて上記
各排出ラインのバルブを開閉制御する制御部とを備えた
ことを特徴とする液分離排出装置。
1. A water tank into which a mixture of two or more liquids having different specific gravities and viscosities flows, a discharge line for discharging an upper liquid and a lower liquid separated in the water tank, and a discharge line for the upper liquid A rotary viscometer that detects the liquid level height and the liquid level height of the lower layer liquid by a change in the rotation speed or rotational resistance of a rotor having different installation heights, and each separated liquid detected by the rotary viscometer. A control unit for controlling the opening and closing of the valves of the respective discharge lines in accordance with the liquid level of the liquid.
【請求項2】 請求項1記載の液分離装置を用いた液分
離方法において、上記水槽内で層分離した上層液と下層
液の液面高さがそれぞれ各回転型粘度計の回転子に達し
たときに上記各排出ラインのバルブを開いてそれぞれの
分離液を排出し、その後、各液面が回転子のレベルを下
回ったときに上記各排出ラインのバルブを閉じて排出を
停止するようにしたことを特徴とする液分離排出方法。
2. The liquid separating method using the liquid separating apparatus according to claim 1, wherein the liquid levels of the upper liquid and the lower liquid separated in the water tank reach the rotors of the respective rotary viscometers. Open the valves of the respective discharge lines to discharge the respective separated liquids, and then close the valves of the respective discharge lines to stop the discharge when the respective liquid levels fall below the level of the rotor. A liquid separation and discharge method, characterized in that:
JP07832699A 1999-03-23 1999-03-23 Liquid separation / discharge device and liquid separation / discharge method Expired - Fee Related JP4348766B2 (en)

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JP07832699A JP4348766B2 (en) 1999-03-23 1999-03-23 Liquid separation / discharge device and liquid separation / discharge method

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JP2000262807A true JP2000262807A (en) 2000-09-26
JP4348766B2 JP4348766B2 (en) 2009-10-21

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* Cited by examiner, † Cited by third party
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WO2004026450A1 (en) * 2002-09-18 2004-04-01 John Raymond Morandini Apparatus for separating out a first liquid component from a mixture with a second heavier liquid component
US7678285B2 (en) 2005-09-19 2010-03-16 Claes Olofsson Apparatus and method for separation of water from an emulsion or mixture of water and oil
KR200453073Y1 (en) 2009-05-28 2011-04-12 인제대학교 산학협력단 Waterbody Diffusers for Density Layer Composition in Baths
KR101574665B1 (en) * 2013-12-05 2015-12-04 신흥정공(주) System and method for separating and filtering of two fluids
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004026450A1 (en) * 2002-09-18 2004-04-01 John Raymond Morandini Apparatus for separating out a first liquid component from a mixture with a second heavier liquid component
US7678285B2 (en) 2005-09-19 2010-03-16 Claes Olofsson Apparatus and method for separation of water from an emulsion or mixture of water and oil
KR200453073Y1 (en) 2009-05-28 2011-04-12 인제대학교 산학협력단 Waterbody Diffusers for Density Layer Composition in Baths
KR101574665B1 (en) * 2013-12-05 2015-12-04 신흥정공(주) System and method for separating and filtering of two fluids
CN109354116A (en) * 2018-11-20 2019-02-19 管庆芬 A kind of oil removing skimmer device for sewage treatment plant
CN110201423A (en) * 2019-04-28 2019-09-06 袁承轩 A kind of automatic water cut-off device based on rotary process
CN110201423B (en) * 2019-04-28 2024-05-03 袁承轩 Automatic water cutting device based on rotation method
KR20230075134A (en) * 2021-11-22 2023-05-31 장섭근 Mixed liquid separator
WO2023090649A3 (en) * 2021-11-22 2024-01-18 장섭근 Device for separating mixed solution
KR102656825B1 (en) * 2021-11-22 2024-04-11 장섭근 Mixed liquid separator
CN116764278A (en) * 2022-05-19 2023-09-19 嘉兴碳捕快科技有限公司 Liquid-liquid phase separation device, liquid-liquid phase automatic separation system and control method thereof

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