JPS6287264A - Discharge method in oil purifier - Google Patents

Discharge method in oil purifier

Info

Publication number
JPS6287264A
JPS6287264A JP22702585A JP22702585A JPS6287264A JP S6287264 A JPS6287264 A JP S6287264A JP 22702585 A JP22702585 A JP 22702585A JP 22702585 A JP22702585 A JP 22702585A JP S6287264 A JPS6287264 A JP S6287264A
Authority
JP
Japan
Prior art keywords
water
oil
pressure
sludge
valve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP22702585A
Other languages
Japanese (ja)
Inventor
Akihide Kato
加藤 明英
Takeo Abe
阿部 武夫
Tomoaki Kato
友明 加藤
Kazutoshi Komaki
小牧 一俊
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.)
Mitsubishi Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha 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 Mitsubishi Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to JP22702585A priority Critical patent/JPS6287264A/en
Publication of JPS6287264A publication Critical patent/JPS6287264A/en
Pending legal-status Critical Current

Links

Landscapes

  • Centrifugal Separators (AREA)

Abstract

PURPOSE:To change the opening and closing time of a valve cylinder and to regulate the discharge amt. of sludge and separated water by changing the pressure of working water on the basis of the signal of a water content detector at the purified oil outlet passage of a rotor. CONSTITUTION:With respect to the method for purifying oil by a centrifugal separator contg. plural separation plates in its rotor, the water content is detected at an optional position of the purified oil B outlet passage of the rotor 1 by the change in the dielectric constant. The signal is transmitted to a controller 6 wherein the water contents in the purified oil B are compared and a selector valve 9 is changed over to the compressed air E2 side at pressure P2 in case of abnormality. Consequently, the compressed air E2 at pressure P2 is supplied to a water tank 8, a cylinder 3 is operated for a longer time than usual, and the sludge C and the water D at the space part are discharged.

Description

【発明の詳細な説明】 産業上の利用分野) 本発明は、回転体中に複数の分離板を内蔵した遠心分離
機で油を清浄化する方法に関し、更に詳細には回転体内
に蓄積したスラッジ及び分離水の排出量を調節する方法
に関するものである。
Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a method for cleaning oil using a centrifugal separator having a plurality of separators built into a rotating body, and more specifically to a method for cleaning oil by cleaning oil using a centrifugal separator having a plurality of separation plates built into a rotating body. and a method for regulating the amount of separated water discharged.

従来技術) 石油/ヨク以降の急激な石油価格の高騰、ならびに1軽
質油(ガンリン、灯油、軽油など)の需要増加に伴ない
、特に船舶に供給される燃料油は低質粗悪化している。
Prior Art) With the rapid rise in oil prices since 1999 and the increase in demand for light oils (ganlin, kerosene, diesel oil, etc.), the quality of fuel oil supplied to ships in particular has been deteriorating.

低質粗悪化している燃料油はより高比重、高粘度となる
傾向にあり、比らの油を清浄化するため遠心分離機が多
く用いられている。特に分離板を内蔵した遠心分離機(
以下分離板型遠心分離機という)は、水分やスラッジな
どの夾雑物の分離性能が高く、且つ保守が容易で自動運
転が可能なため広く用いられている。前記分離板型遠心
分離機は被処理油の性状によって、軽液(清浄油)−重
液(分離水)−固形物(スラッジ)の三層として分離す
る三層遠心分離機(以下ビュリファイアという)として
使用される場合と、軽液(清浄油)−夾雑物(重液と固
形物)の二層として分離する二層遠心分離機(以下タラ
リファイアという)として使用される場合があり、本発
明は後者のタラリファイアに関するものである。
Fuel oil that has deteriorated in quality and quality tends to have higher specific gravity and higher viscosity, and centrifugal separators are often used to purify this oil. Especially centrifuges with built-in separators (
BACKGROUND ART Separation plate centrifuges (hereinafter referred to as separator plate centrifuges) are widely used because they have high performance in separating impurities such as moisture and sludge, are easy to maintain, and can be operated automatically. The separation plate type centrifuge is a three-layer centrifuge (hereinafter referred to as a burifier) that separates the oil into three layers: light liquid (clean oil) - heavy liquid (separated water) - solid matter (sludge) depending on the properties of the oil to be processed. ), and as a double-layer centrifuge (hereinafter referred to as a "talarifier") that separates light liquid (clean oil) and impurities (heavy liquid and solids) into two layers. The invention relates to the latter talarifier.

発明が解決しようとする問題点) 従来のビュリファイアでは、油と水の比重差が少なくな
り、被処理油の比重が099/ (at /j/ II
℃)以上となると、回転体内の清浄油と分離水の分離境
界面が不安定となる。従って分離水の抜き出し位置を調
節する調節板の交換を頻繁に行なわなければならず、安
定した運転が困難であった。
Problems to be Solved by the Invention) In conventional burifiers, the difference in specific gravity between oil and water is small, and the specific gravity of the oil to be treated is 099/ (at /j/ II
℃) or higher, the separation interface between the clean oil and separated water in the rotating body becomes unstable. Therefore, the adjustment plate that adjusts the position from which the separated water is extracted must be replaced frequently, making stable operation difficult.

又前記状態の場合には、通常タラリファイアが使用され
るが、従来のタラリファイアでは、分離水を連続的に排
出することができないため、回転体内の許容スペース以
上に分離水が溜ると清浄油側へ回り込み、清浄油中に水
分が混入する欠点があった。又前記状態で運転を続ける
と、分離境界面は回転体の内側の分離板層へ寄ってしま
い、分離効果が著しく悪くなる。前記の欠点を補うもの
としては、回転体の弁7リンダーの開閉時間を極度に短
かくシ、回転体内へ蓄積されたスラッジや分離水の一部
を頻繁に排出する装置があるが、弁パツキンの摩耗を早
め回転体からの油の漏洩や、又排出間隔、排出時間及び
作動水圧力が固定されているため、常に一定景しか排出
されず、被処理液中に含有するスラッジ及び水分の含有
量が変動した場合には、此れに追従できない等の欠点が
あつだ。
In addition, in the case of the above condition, a tarlarifier is usually used, but since the conventional tarlarifier cannot continuously discharge the separated water, if the separated water accumulates beyond the allowable space inside the rotating body, the clean oil will be removed. There was a drawback that moisture could get mixed into the clean oil. Further, if the operation is continued under the above conditions, the separation boundary surface will approach the separation plate layer inside the rotating body, and the separation effect will be significantly deteriorated. To compensate for the above drawbacks, there is a device that extremely shortens the opening and closing time of the valve 7 cylinder of the rotating body and frequently discharges part of the sludge and separated water accumulated in the rotating body. This can lead to faster wear and oil leakage from the rotating body, and because the discharge interval, discharge time, and working water pressure are fixed, only a certain amount of water is discharged at all times, and the sludge and moisture contained in the liquid to be treated can be easily discharged. If the amount fluctuates, it has drawbacks such as not being able to follow it.

問題点を解決するだめの手段) 本発明は、前記の!■情に鑑みてなされたものであり、
分離板型遠心分離機で油を清浄化する方法において、回
転体の7/I浄油出ロ流路に設けた水分検知装置からの
信号で回転体弁ンリンダーを開閉作動させる作動水の水
圧を変圧することにより、前記弁シリ7ダーの開閉時間
を変更し、スラッジ及び分離水の排出量を調節すること
を特徴とする油清浄装置の排出方法である。前記の本発
明において通常は、従来のようにタイマーで設定された
排出間隔、排出時間により弁/す/ダーの開閉が行なわ
れ、スラッジ等を排出する操作が併用される。水分検知
装置は、静電容量式、濁度式等油と水分の物性差を検知
するものであればよい。
(Means for Solving the Problem) The present invention is directed to the above-mentioned! ■It was done out of consideration for the circumstances;
In the method of cleaning oil using a separator plate centrifuge, the water pressure of the operating water that opens and closes the valve and cylinder of the rotor is controlled by a signal from a moisture detection device installed in the 7/I purified oil outlet flow path of the rotor. This is a method for discharging an oil cleaning device, characterized in that the opening and closing time of the valve cylinder 7 is changed by changing the pressure, and the discharge amount of sludge and separated water is adjusted. In the above-mentioned invention, normally, the valve/sump/der is opened and closed according to the discharge interval and discharge time set by a timer as in the conventional method, and the operation for discharging sludge and the like is also used. The moisture detection device may be one that detects the difference in physical properties between oil and moisture, such as a capacitance type or a turbidity type.

作動水の圧力を変圧する方法としては、空気加圧式水夕
/りを用い供給空気圧力を制御してもよく、又圧力の違
う複数の作動水供給系統を設は切り換えるようにしても
よい。
As a method for changing the pressure of the working water, an air pressurized water tank may be used to control the supply air pressure, or a plurality of working water supply systems having different pressures may be installed and switched.

作  用 ) 被処理油中の水分が多い場合、又は多くなった場合には
回転体内に蓄積された分離水が分離板層に達し′rIl
争油中の水分景が急激に上昇する。この現象を水分検知
装置により検知し、信号を検知装置コントローラを経て
自動制御盤へ送り、該制御盤によって弁シリンダーの開
閉作動をする作動水の圧力を通常の圧力以上に変更させ
る。作動水圧力が高くなると開弁水排出用ノズルからの
単位時間当りの作動水排出量も増加するがそれ以上の作
動水量が実質供給され作動水の作動時間も長くなる。従
って弁シリンダーの開時間が通常より長くなり、排出量
も多くなる。
Effect) When there is a lot of water in the oil to be treated, or if it becomes too much, the separated water accumulated in the rotating body will reach the separating plate layer.
The water level in the oil race rises rapidly. This phenomenon is detected by the moisture detection device, and a signal is sent via the detection device controller to the automatic control panel, which changes the pressure of the working water that opens and closes the valve cylinder to a level higher than the normal pressure. As the working water pressure increases, the amount of working water discharged per unit time from the open valve water discharge nozzle also increases, but a larger amount of working water is actually supplied and the operating time of the working water also becomes longer. Therefore, the opening time of the valve cylinder is longer than usual, and the amount of discharge is also increased.

実  施  例 ) 以下図面に示した実施例に基づいて本発明の詳細な説明
する。第1図は本発明の一実施例を示す系統図、第1図
は回転体要部の縦断面図である。
Embodiments) The present invention will be described in detail below based on embodiments shown in the drawings. FIG. 1 is a system diagram showing one embodiment of the present invention, and FIG. 1 is a longitudinal sectional view of the main parts of a rotating body.

lは分離板型遠心分離機の回転体であり、槙層した複数
の分離板−を内蔵しており毎分数千回転の速度で回転す
る。3は回転体/の下部に設けられ作動水Fにより作動
するパイロット弁機構により上下摺動し、スラッジ分離
水を排出するだめの排出孔lの開閉を行なう弁シリンダ
ーである。当該弁シリンダーの開閉によるスラッジ排出
工程は、まず作動水Fを閉弁水圧室lλに導入し、閉弁
水圧室/2が満杯になるとオーバーフローし開弁水圧室
10へ流入する。開弁水圧室10に作動水Fが充満する
とパイロット弁l/を反半径方向に摺動して閉弁水排出
用ノズル/lのパツキン部の7−ルが破れ閉弁水の一部
が回転体外へ流出し回転体内圧力により弁ンリンダー3
が押し下げられ排出孔グが開放してスラッジ排出が行な
われる。開弁水圧室IOの作動水Fは開井水排出用ノズ
ル/3から抜は出てパツキン部が7−ルされ作動水Fが
閉弁水圧室/、!に充満し、弁シリンダー3が押し上げ
られ排出孔グが閉塞されてスラッジ排出工程が終了する
。前記の工程をタイマーにより一定間隔で繰り返えす。
1 is a rotating body of a separator plate type centrifugal separator, which includes a plurality of layered separator plates and rotates at a speed of several thousand revolutions per minute. Reference numeral 3 denotes a valve cylinder which is provided at the bottom of the rotating body / and is slid up and down by a pilot valve mechanism operated by working water F to open and close the discharge hole 1 for discharging the sludge separated water. In the sludge discharge process by opening and closing the valve cylinder, first, working water F is introduced into the valve-closing hydraulic chamber lλ, and when the valve-closing hydraulic chamber /2 becomes full, it overflows and flows into the valve-opening hydraulic chamber 10. When the valve-opening water pressure chamber 10 is filled with working water F, the pilot valve l/ is slid in the opposite radial direction, and the gasket part 7 of the valve-closing water discharge nozzle/l is ruptured, causing a part of the valve-closing water to rotate. It flows out of the body and due to the pressure inside the rotating body, the valve cylinder 3
is pushed down, the discharge hole opens, and the sludge is discharged. The working water F in the open-valve hydraulic chamber IO is drawn out from the open-well water discharge nozzle /3, the seal part is sealed, and the working water F enters the closed-valve hydraulic chamber /,! The valve cylinder 3 is pushed up, the discharge hole is closed, and the sludge discharge process is completed. The above steps can be repeated at regular intervals using a timer.

jは比誘電率の変化により水分の含量を検知する静電容
量式の水分検知装置であり清浄油Bの出口経路の任意位
置に設けられる。gは空気加圧式の水タンクで作動水F
が貯留されており上部空気の圧力により作動水圧を制御
する。りは前記水タンク♂へ圧力P/の空気Fi/とそ
れより高い圧力P−の空気E2 を切り換えて送入する
切換弁である。被処理液Aは回転体/の原液入口から回
転体/内へ供給され、供給された被処理QAは遠心力と
分離板!の作用により清浄油BとスラッジC及び分離水
りに分離される。分離された清浄油Bは分離板間を上昇
し清浄油Bの出口から導出され、又スラッジCと分離水
りは分離板端より外側のスペースSへ蓄積されていく。
j is a capacitance-type moisture detection device that detects the moisture content based on a change in dielectric constant, and is provided at an arbitrary position on the outlet path of the clean oil B. g is the operating water F in an air pressurized water tank.
is stored, and the operating water pressure is controlled by the pressure of the upper air. This is a switching valve that switches and sends air Fi/ at a pressure P/ and air E2 at a higher pressure P- to the water tank ♂. The liquid to be treated A is supplied into the rotating body from the stock solution inlet of the rotating body, and the supplied liquid to be treated QA is affected by centrifugal force and separation plate! is separated into clean oil B, sludge C, and separated water. The separated clean oil B rises between the separation plates and is led out from the outlet of the clean oil B, and the sludge C and separated water accumulate in the space S outside the ends of the separation plates.

通常の運転においては、スラッジCや分離水りがスペー
スS/まで蓄積されたときに、圧力P/の圧力空気E/
を水タンク!へ供給して、圧力がP/の作動水E/で弁
シリンダ−3を開作動させ、スペースS1分だけスラッ
ジCと分離水りを排出孔グから排出する。又前記は自動
制御盤7に設けられたタイマーにより事前に設定された
排出間隔で行なわれる。被処理油A中に水分が多い場合
又は性状が変動し水分が多くなった場合には、前記タイ
マーによる排出間隔だけでは追従できず、分離水りがス
ペースS2 を越えて清浄油B中へ混入し清浄油B中の
水分量を急激に上昇させる。清浄油出口流路に設けられ
た水分検知装置jからの検知信号が常に検知装置コント
ローラtへ送信され設定された範囲の水分量との比較が
行なわれている。従って前記状態になると比誘電率が急
激に上昇し水分検知装置jからの検知信号は、検知装置
コントローラ乙により異常値として判断され、当該コン
トローラ2から切換弁りを圧力P2の圧力空気E2側へ
切換える信号が自動操作盤7へ発信される。圧力P、2
の圧力空気E2を水タンクgへ供給することにより、圧
力がP、!の作動水Elで弁ンリンダー3を通常より長
い時間開作動させスペースS/+82分のスラッジCと
分離水りを排出孔グから排出する。
In normal operation, when sludge C and separated water accumulate up to space S/, pressurized air E/ of pressure P/
A water tank! The valve cylinder 3 is opened with working water E/ having a pressure of P/, and the sludge C and separated water are discharged from the discharge hole by a space S1. Further, the above-described process is performed at preset discharge intervals by a timer provided in the automatic control panel 7. If there is a lot of water in the oil A to be treated, or if the water content increases due to changes in its properties, it will not be possible to keep up with the discharge interval by the timer, and the separated water will cross the space S2 and mix into the clean oil B. The amount of water in clean oil B is rapidly increased. A detection signal from a moisture detection device j provided in the clean oil outlet flow path is constantly transmitted to a detection device controller t and compared with a moisture amount within a set range. Therefore, when the above condition occurs, the relative permittivity increases rapidly, and the detection signal from the moisture detection device j is judged as an abnormal value by the detection device controller B, and the controller 2 directs the switching valve to the pressure air E2 side of the pressure P2. A switching signal is sent to the automatic operation panel 7. Pressure P, 2
By supplying pressurized air E2 to the water tank g, the pressure increases to P,! The valve cylinder 3 is opened for a longer time than usual using the working water El, and the sludge C and separated water corresponding to the space S/+82 are discharged from the discharge hole.

効  果 ) /)従来のビュリファイアのように、調節板の厳密なる
選定や、頻繁な交換が不要であり、被処理油中の水分量
変動にも容易に追従することができる。
Effects) /) Unlike conventional burifiers, there is no need for strict selection of adjustment plates or frequent replacement, and it can easily follow fluctuations in the amount of water in the oil to be treated.

2)従来のタラリファイアのように、分離水が回転体内
の許容スペース以上に溜まり清浄油へ混入し分離効率を
低下させることがない。
2) Unlike conventional tararifiers, separated water does not collect in an amount larger than the allowable space within the rotating body and mix into clean oil, reducing separation efficiency.

3)スラッジ及び分離水の排出量(排出時間)を運転中
に調節する方法において、従来の作動水の作動時間をタ
イマーにより変更する方法では1秒以内の調整となるた
め困難であるが、本発明では、作動水圧力を変圧して作
動時間を変更する方法を用いているので容易である。
3) Regarding the method of adjusting the discharge amount (drainage time) of sludge and separated water during operation, the conventional method of changing the operating time of working water using a timer requires adjustment within 1 second, which is difficult, but this method The invention is easy because it uses a method of changing the operating time by changing the operating water pressure.

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

第1図は本発明の一実施例の系統図、第2図は回転体要
部の縦断面図である。 /:回転体1.2:分離板、3:弁シリンダ−、l:排
出孔、!:水分検知装置、t:検知装置コントローラ、
7:自動制御盤、g:水タンク、9:切換弁、10:開
弁水圧室、//:ハイロット弁、/λ:閉弁水圧室、/
3:開弁水排出用ノズル、/り:閉弁水排出用ノズル、
A:被処理油、B:清浄油、C:スラッジ、D:分離水
、ESK/、E、!:圧力空気、F:作動水。
FIG. 1 is a system diagram of an embodiment of the present invention, and FIG. 2 is a longitudinal sectional view of the main parts of a rotating body. /: Rotating body 1.2: Separation plate, 3: Valve cylinder, l: Discharge hole, ! : moisture detection device, t: detection device controller,
7: automatic control panel, g: water tank, 9: switching valve, 10: open valve hydraulic chamber, //: high lot valve, /λ: close valve hydraulic chamber, /
3: Open valve water discharge nozzle, /ri: Closed valve water discharge nozzle,
A: Oil to be treated, B: Clean oil, C: Sludge, D: Separated water, ESK/, E,! : Pressure air, F: Working water.

Claims (1)

【特許請求の範囲】[Claims] 回転体中に複数の分離板を内蔵し、且つ作動水により開
閉作動する弁シリンダーを具備した遠心分離機で油を清
浄化する方法において、前記回転体の清浄油出口流路に
設けた水分検知装置からの信号で前記作動水の水圧を変
圧することにより、前記弁シリンダーの開閉時間を変更
し、スラッジ及び分離水の排出量を調節することを特徴
とする油清浄装置の排出方法。
In a method for cleaning oil using a centrifugal separator that has a plurality of separation plates built into a rotating body and is equipped with a valve cylinder that is opened and closed by operating water, a moisture detection device provided in a clean oil outlet flow path of the rotating body A method for discharging an oil purifying device, characterized in that the opening/closing time of the valve cylinder is changed by changing the pressure of the working water in response to a signal from the device, thereby adjusting the amount of sludge and separated water to be discharged.
JP22702585A 1985-10-14 1985-10-14 Discharge method in oil purifier Pending JPS6287264A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22702585A JPS6287264A (en) 1985-10-14 1985-10-14 Discharge method in oil purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22702585A JPS6287264A (en) 1985-10-14 1985-10-14 Discharge method in oil purifier

Publications (1)

Publication Number Publication Date
JPS6287264A true JPS6287264A (en) 1987-04-21

Family

ID=16854333

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22702585A Pending JPS6287264A (en) 1985-10-14 1985-10-14 Discharge method in oil purifier

Country Status (1)

Country Link
JP (1) JPS6287264A (en)

Similar Documents

Publication Publication Date Title
KR870001593B1 (en) Centrifugal separator and method of operating the same
RU2393024C2 (en) Centrifugal separator and method of separation
SU1572402A3 (en) Centrifugal separator
US3938734A (en) Controlling system for the displacement of the specifically lighter liquid components from a self-emptying separator
KR20030007493A (en) Backflush filter, in particular for filtering lubricant oil
JP4397516B2 (en) Separator plate centrifuge and method for operating the same
JP5386641B2 (en) Separator plate centrifuge and method for operating the same
US1866638A (en) Centrifugal separator
US4069969A (en) Automatic three stage centrifugal sludge separator
JPS6287264A (en) Discharge method in oil purifier
JP4592934B2 (en) Separator plate centrifuge and method for operating the same
US5507955A (en) Method of operating hydrocyclone systems by adding water to maintain flow rates
JP4516175B2 (en) Separator centrifuge
CN115822065A (en) Water level self-regulating valve drainage system
JPH07246349A (en) Separation plate type centrifuge
JP4516174B2 (en) Separator centrifuge
JP2725868B2 (en) Centrifuge with pump means for producing circulating flow
JP2554908B2 (en) How to operate the centrifuge
KR0127594Y1 (en) Regenerative apparatus of rapid band filter basin
US20240253058A1 (en) Method and system for purification of oil
JPS60220157A (en) Centrifugal separation apparatus
KR20240053665A (en) filter device
JPS637809A (en) Separator for coarse particle contained in slurry
JPS60166055A (en) Oil purifier
JP2024531617A (en) Filter Device