JPH03181348A - Method for cleaning separation plate-type centrifugal separator - Google Patents
Method for cleaning separation plate-type centrifugal separatorInfo
- Publication number
- JPH03181348A JPH03181348A JP32208689A JP32208689A JPH03181348A JP H03181348 A JPH03181348 A JP H03181348A JP 32208689 A JP32208689 A JP 32208689A JP 32208689 A JP32208689 A JP 32208689A JP H03181348 A JPH03181348 A JP H03181348A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- cleaning liquid
- water outlet
- flow rate
- liquid
- 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
Links
- 238000004140 cleaning Methods 0.000 title claims abstract description 185
- 238000000034 method Methods 0.000 title claims abstract description 17
- 238000000926 separation method Methods 0.000 title claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000007788 liquid Substances 0.000 claims description 122
- 230000000694 effects Effects 0.000 abstract description 13
- 239000003921 oil Substances 0.000 description 23
- 239000010802 sludge Substances 0.000 description 21
- 238000005406 washing Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 4
- 239000011550 stock solution Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B15/00—Other accessories for centrifuges
- B04B15/06—Other accessories for centrifuges for cleaning bowls, filters, sieves, inserts, or the like
Landscapes
- Centrifugal Separators (AREA)
Abstract
Description
【発明の詳細な説明】
イ9発明の目的
〔産業上の利用分野〕
この発明は、回転体内に多数の分離板を互いに間隔を空
けて設けた分離板型遠心分離機(以下、単に遠心分離機
という)の回転体に洗浄液を循環させ、回転体の内部部
品の表面に付着しているスラッジ(不溶解性)等の有害
物質を洗浄除去する方法に関するものである。Detailed Description of the Invention A9.Objective of the Invention [Field of Industrial Application] This invention relates to a separating plate type centrifuge (hereinafter simply referred to as a centrifugal separator) in which a large number of separating plates are provided at intervals in a rotating body. This relates to a method for cleaning and removing harmful substances such as sludge (insoluble) adhering to the surface of the internal parts of the rotating body by circulating a cleaning liquid through the rotating body of the rotating body.
分離板型遠心分離機は、船舶用、陸上用ディーゼル機関
の燃料油及び潤滑油の清浄に使用されている。この遠心
分離機には、分離したスラッジを排出する機構も備えて
いるが、長時間使用していると、分離したスラッジが完
全に排出されずに分離板及び回転体内部部品表面に蓄積
されてくる。Separating plate centrifuges are used to clean fuel oil and lubricating oil for marine and land-based diesel engines. This centrifugal separator is also equipped with a mechanism to discharge separated sludge, but when used for a long time, the separated sludge is not completely discharged and accumulates on the surface of the separating plate and internal parts of the rotating body. come.
そこで遠心分離機の洗浄が必要となってくる。Therefore, it becomes necessary to clean the centrifuge.
従来、遠心分離機の洗浄は、第1図に示す洗浄装置によ
って、次のように行っている。Conventionally, centrifugal separators have been cleaned in the following manner using a cleaning device shown in FIG.
洗浄液は、洗浄液タンク5から送液体ポンプ6、流量制
御弁8を経て遠心分離機lの原液入口2に供給され、遠
心分離機lの油出口3及び水出口4を通って洗浄液タン
ク5に戻される。即ち、洗浄液は、洗浄液タンク5−遠
心分離機l→洗浄液タンク5を循環し、遠心分離機Iを
洗浄する。なお、水出口4から洗浄液タンク5への流路
の途中には制御弁14が設けである。The cleaning liquid is supplied from the cleaning liquid tank 5 to the raw liquid inlet 2 of the centrifugal separator 1 via the liquid sending pump 6 and the flow rate control valve 8, and is returned to the cleaning liquid tank 5 through the oil outlet 3 and water outlet 4 of the centrifugal separator 1. It will be done. That is, the cleaning liquid circulates from the cleaning liquid tank 5 to the centrifuge I and then through the cleaning liquid tank 5 to clean the centrifuge I. Note that a control valve 14 is provided in the middle of the flow path from the water outlet 4 to the cleaning liquid tank 5.
洗浄液の循環量は、送液体ポンプ6の能力により決定さ
れ、回転体内の汚れを十分に洗浄するためには大容量の
送液体ポンプ6を必要とするが、それは洗浄装置の経済
性から不利であるので、現実には低容量の送液体ポンプ
6を用いている。The circulation amount of the cleaning liquid is determined by the capacity of the liquid pump 6, and in order to sufficiently clean the dirt inside the rotating body, a large capacity liquid pump 6 is required, but this is disadvantageous from the economical point of view of the cleaning device. Therefore, in reality, a low-capacity liquid feeding pump 6 is used.
低容Qの送液ポンプ6を用い、遠心分離機lと洗浄族タ
ンク5との間に洗浄液を循環させて洗浄する従来の遠心
分離機の洗浄においては、水出口4側の制御弁14を絞
って、流量抵抗の効果により、油出口3側にも洗浄液を
吐出させようとしているが、流量が少ないためにその効
果が得られず、はとんどの場合、洗浄液の全量が水出口
4より吐出され、回転体内部の中央部及び油出口3側を
洗浄することができなかった。同時に、汚れのきつい水
出口4側通路部品も、流量不足のため十分な洗浄がなさ
れない欠点がある。In conventional centrifuge cleaning, in which cleaning is performed by circulating cleaning liquid between the centrifuge 1 and the cleaning group tank 5 using a liquid sending pump 6 with a low volume Q, the control valve 14 on the water outlet 4 side is closed. By squeezing the flow, the cleaning liquid is also discharged to the oil outlet 3 side due to the effect of flow resistance, but this effect cannot be obtained because the flow rate is small, and in most cases, the entire amount of cleaning liquid is discharged from the water outlet 4. The oil was discharged, and the central part inside the rotor and the oil outlet 3 side could not be cleaned. At the same time, there is a drawback that the heavily contaminated water outlet 4 side passage parts cannot be sufficiently cleaned due to insufficient flow rate.
この発明は、分離板及び回転体内部部品表面に付着、蓄
積したスラッジを洗浄液を用いて洗浄する場合に、経済
的に安価で且つ技術的に安易な方法で洗浄効果を高める
洗浄方法を提供することを目的としている。The present invention provides a cleaning method that improves the cleaning effect in an economically inexpensive and technically easy method when cleaning sludge that adheres to and accumulates on the surface of a separator plate and internal parts of a rotating body using a cleaning liquid. The purpose is to
a1発明の構成
〔課題を解決するための手段〕
上記目的を達成するために、この発明の分離板型遠心分
離機の洗浄方法においては、洗浄液タンク5の洗浄液を
送液ポンプ6によって遠心分離機lの原液入口2に注入
し、遠心分離機1の油出口3及び水出口4から吐出され
る洗浄液を再び洗浄液タンク5に戻す配管系路と、水出
口4から吐出される洗浄液を遠心分離機工内部のペアリ
ングディスクポンプ20によって直接原液入口2に戻す
配管系路とを有する洗浄装置を用い、水出口4から吐出
される洗浄液を直接原液入口2に戻す高流量洗浄と、遠
心分離機1と洗浄液タンク5との間に洗浄液を循環させ
る低流量洗浄とに切替えるものである。a1 Structure of the Invention [Means for Solving the Problems] In order to achieve the above object, in the method for cleaning a separating plate centrifuge of the present invention, the cleaning liquid in the cleaning liquid tank 5 is transferred to the centrifuge by the liquid feeding pump 6. The cleaning liquid injected into the raw solution inlet 2 of the centrifuge 1 and discharged from the oil outlet 3 and water outlet 4 of the centrifuge 1 is returned to the cleaning liquid tank 5, and the cleaning liquid discharged from the water outlet 4 is transferred to the centrifugal separator. Using a cleaning device having a piping system that returns the cleaning liquid directly to the raw solution inlet 2 by an internal pairing disk pump 20, high-flow cleaning is performed in which the cleaning liquid discharged from the water outlet 4 is returned directly to the raw solution inlet 2, and a centrifuge 1 is used. This is to switch to low flow rate cleaning in which the cleaning liquid is circulated between the cleaning liquid tank 5 and the cleaning liquid tank 5.
上記のように構成された分離板型遠心分離機の洗浄方法
は、最初の高流量洗浄においては、洗浄液は、送液ポン
プ6によって洗浄液タンク5から遠心分離機1へ送られ
、油出口3及び水出口4から吐出され、水出口4から吐
出された洗浄液は、遠心分離機1内部のペアリングディ
スクポンプ20によって直接原液入口2に戻される。続
く低流量洗浄においては、洗浄液は、送液ポンプ6によ
って洗浄液タンク5から遠心分離機1へ送られ、水出口
4から吐出され、遠心分離機lと洗浄液タンク5との間
を循環する。このとき、油出口3からの洗浄液の吐出は
ない。In the cleaning method for the separator plate type centrifugal separator configured as described above, in the first high flow rate cleaning, the cleaning liquid is sent from the cleaning liquid tank 5 to the centrifugal separator 1 by the liquid sending pump 6, and the oil outlet 3 and The cleaning liquid discharged from the water outlet 4 is directly returned to the stock solution inlet 2 by a pairing disk pump 20 inside the centrifugal separator 1 . In the subsequent low flow rate cleaning, the cleaning liquid is sent from the cleaning liquid tank 5 to the centrifugal separator 1 by the liquid sending pump 6, discharged from the water outlet 4, and circulated between the centrifugal separator 1 and the cleaning liquid tank 5. At this time, no cleaning liquid is discharged from the oil outlet 3.
この発明の洗浄方法に使用する洗浄装置の一例を第3図
を参照して説明する。An example of a cleaning device used in the cleaning method of the present invention will be explained with reference to FIG.
1は遠心分離機であり、5は洗浄液タンクである。洗浄
液タンク5と遠心分離機】の原液入口2との間に送液管
9を設けている。その送液管9には、送液ポンプ6、逆
止弁7、洗浄液入口支管I11流量調整弁8を洗浄タン
ク5より順に取付ける。遠心分離機1の出口側の油出口
3には、洗浄液タンク5に戻す油出口管13を、水出口
4には、水出口管18をそれぞれ設ける。その水出口管
18には、制御弁14、三方制御弁17を水出口4より
順に取付ける。三方制御弁17から、流量調整弁8と原
液入口2との間の送液管9へは、循環管16が接続され
ており、三方制御弁17は、循環管16側と、洗浄液タ
ンク5に戻す洗浄液タンク戻し管15側とに、洗浄液の
流路を任意切替えるためのるものである。なお、この三
方制御弁17に代えて、洗浄液タンク戻し管15及び循
環管16のそれぞれに開閉弁を設けてもよいことはいつ
までもない。1 is a centrifugal separator, and 5 is a washing liquid tank. A liquid feed pipe 9 is provided between the cleaning liquid tank 5 and the stock liquid inlet 2 of the centrifugal separator. A liquid feeding pump 6, a check valve 7, a cleaning liquid inlet branch pipe I11 and a flow rate adjustment valve 8 are attached to the liquid feeding pipe 9 in this order from the cleaning tank 5. The oil outlet 3 on the outlet side of the centrifugal separator 1 is provided with an oil outlet pipe 13 for returning to the cleaning liquid tank 5, and the water outlet 4 is provided with a water outlet pipe 18. A control valve 14 and a three-way control valve 17 are attached to the water outlet pipe 18 in order from the water outlet 4. A circulation pipe 16 is connected from the three-way control valve 17 to the liquid supply pipe 9 between the flow rate adjustment valve 8 and the stock solution inlet 2. The three-way control valve 17 is connected to the circulation pipe 16 side and the cleaning liquid tank 5. This is provided to arbitrarily switch the flow path of the cleaning liquid to the cleaning liquid tank return pipe 15 side. Note that instead of the three-way control valve 17, an on-off valve may be provided in each of the cleaning liquid tank return pipe 15 and the circulation pipe 16.
送液ポンプ6により、遠心分離機1に供給され、その油
出口3から吐出される洗浄液は、洗浄液タンク5に戻さ
れ、水出口4から吐出される洗浄液は、三方制御弁17
により、洗浄液タンク5に戻すラインと送液管9に戻す
ラインに切替えられ、それぞれ循環システムが構成され
る。The cleaning liquid supplied to the centrifugal separator 1 by the liquid sending pump 6 and discharged from the oil outlet 3 is returned to the cleaning liquid tank 5, and the cleaning liquid discharged from the water outlet 4 is supplied to the centrifugal separator 1 by the three-way control valve 17.
As a result, the line is switched to the line returning to the cleaning liquid tank 5 and the line returning to the liquid feeding pipe 9, thereby configuring a circulation system.
このような洗浄装置を用いての遠心分離機lの洗浄は、
次のようにして行う。Cleaning the centrifuge l using such a cleaning device is as follows:
Do it as follows.
最初に高流量洗浄を行う。First perform a high flow wash.
先ず、洗浄液タンク5に適量の洗浄液を入れる。水出口
管18の三方制御弁17を循環管16側に設定しておく
。また、送液ポンプ6の流量は、低流量洗浄を想定して
流量調節弁8により低流量に設定しておく。遠心分離機
lを定常運転状態にし、送液ポンプ6を始動し洗浄を開
始する。回転体内に充満した洗浄液は、水出口4より吐
出され、水出口管18、三方制御弁17、循環管16を
通って送液管9に戻され、再び原液入口2より遠心分離
機1に入る高流量循環ラインを流れる。このときの洗浄
液の循環量は、遠心分離機lに装備されているペアリン
グディスクポンプ20の能力を利用するものであり、流
量制御弁8によって定された送液ポンプ6の流量に関係
なく、送液ポンプ6の絞切圧に相当した圧力のペアリン
グディスクポンプ20の流量となる。通常、ペアリング
ディスクポンプ20は、遠心分離機lの能力に見合った
性能を有しており、送液ポンプ6の絞切圧の設定により
、容量の小さな送液ポンプ6でも、高流量循環ラインに
設定したときの洗浄液の流量は、遠心分離機lの臨界流
量に近い高流量となる。First, an appropriate amount of cleaning liquid is put into the cleaning liquid tank 5. The three-way control valve 17 of the water outlet pipe 18 is set on the circulation pipe 16 side. Further, the flow rate of the liquid feeding pump 6 is set to a low flow rate by the flow rate control valve 8 assuming low flow rate cleaning. The centrifugal separator 1 is brought into a steady state of operation, the liquid feed pump 6 is started, and cleaning is started. The cleaning liquid filled in the rotating body is discharged from the water outlet 4, passes through the water outlet pipe 18, the three-way control valve 17, and the circulation pipe 16, returns to the liquid supply pipe 9, and enters the centrifuge 1 again from the stock solution inlet 2. Flows through a high flow circulation line. The circulation amount of the cleaning liquid at this time utilizes the ability of the pairing disk pump 20 installed in the centrifugal separator 1, and is independent of the flow rate of the liquid feeding pump 6 determined by the flow rate control valve 8. The flow rate of the pairing disk pump 20 has a pressure corresponding to the throttling pressure of the liquid feeding pump 6. Normally, the pairing disk pump 20 has performance commensurate with the capacity of the centrifugal separator l, and by setting the throttling pressure of the liquid feeding pump 6, even a liquid feeding pump 6 with a small capacity can be used for high flow rate circulation lines. The flow rate of the cleaning liquid when set to is a high flow rate close to the critical flow rate of the centrifuge l.
このとき、比重板22の条件等によっては、高流量化だ
けでは洗浄液が油出口3から吐出しない場合があり、そ
のときは水出口管18の制御弁14を絞ることにより油
出口3に少量洗浄酸を吐出させることができる。油出口
3より油出口管13に吐出した洗浄液は、洗浄液タンク
5に戻され、その分注浄戒は補充されることになり、高
流量洗浄が維持される。At this time, depending on the conditions of the specific gravity plate 22, cleaning liquid may not be discharged from the oil outlet 3 simply by increasing the flow rate.In that case, by squeezing the control valve 14 of the water outlet pipe 18, a small amount of cleaning liquid can be washed into the oil outlet 3. Acid can be discharged. The cleaning liquid discharged from the oil outlet 3 to the oil outlet pipe 13 is returned to the cleaning liquid tank 5, and its dispensing liquid is replenished, thereby maintaining high flow rate cleaning.
この高流量洗浄を約30〜45分程度行った後に、水出
口管18の三方制御弁17を洗浄液タンク戻し管15側
に切替え、低流量洗浄を行う。After performing this high flow rate cleaning for about 30 to 45 minutes, the three-way control valve 17 of the water outlet pipe 18 is switched to the cleaning liquid tank return pipe 15 side, and low flow rate cleaning is performed.
即ち、水出口4より吐出された洗浄液は、洗浄液タンク
戻し管15により洗浄液タンク5に戻され、洗浄液タン
ク5と遠心分離機lを循環するラインが形成される。こ
のときの洗浄液の循環量は、流量調整弁8で設定された
送液ポンプ6の容量によって定まり、洗浄液は、全量水
出口4より吐出される。この低流量洗浄を約30〜60
9程度行い、洗浄工程は終了する。That is, the cleaning liquid discharged from the water outlet 4 is returned to the cleaning liquid tank 5 through the cleaning liquid tank return pipe 15, forming a line that circulates between the cleaning liquid tank 5 and the centrifugal separator 1. The circulating amount of the cleaning liquid at this time is determined by the capacity of the liquid feeding pump 6 set by the flow rate adjustment valve 8, and the entire amount of the cleaning liquid is discharged from the water outlet 4. This low flow rate cleaning is approximately 30 to 60 minutes.
After about 9 times, the cleaning process is completed.
三方制御弁17の切替えは、タイマーと電動三方弁の組
合せにより容易に自動化することができる。Switching of the three-way control valve 17 can be easily automated by a combination of a timer and an electric three-way valve.
洗浄工程が終了すると、送液ポンプ6を停止し、遠心分
離機lのスラッジ排出作動を行い、回転体内の洗浄液及
びスラッジの排出を行う。次に、清水により回転体内部
の水洗を行う。洗浄水は遠心分離機Iの標準装備の封水
入口から供給するか、もしくは洗浄装置の送液管9の途
中に設けた洗浄水供給弁12より供給する。回転体内に
洗浄水を充満させた後に、スラッジ排出作動を行う。こ
れを2〜3回繰返し、水洗工程を終了する。When the cleaning process is completed, the liquid feed pump 6 is stopped, and the centrifugal separator 1 is operated to discharge the sludge, thereby discharging the cleaning liquid and sludge from the rotating body. Next, the inside of the rotating body is washed with fresh water. Washing water is supplied from a water sealing inlet that is a standard feature of the centrifugal separator I, or from a washing water supply valve 12 provided in the middle of the liquid feed pipe 9 of the washing device. After filling the rotating body with cleaning water, the sludge discharge operation is performed. This is repeated 2 to 3 times to complete the water washing process.
このように、この発明においては、洗浄効果を高めるた
め、高流量洗浄と低流量洗浄の2段洗浄を行っているが
、ここで、第2図及び第3図を参照して2段洗浄の必要
性について説明する。In this way, in this invention, two-stage cleaning of high flow rate cleaning and low flow rate cleaning is performed in order to enhance the cleaning effect. Explain the necessity.
一般に、洗浄液を流して物体の表面に付着したスラッジ
を洗浄する場合、洗浄液の流量が高いほど洗浄効果はよ
い。つまり、高流量洗浄により水出口側部品の洗浄を効
果的に行うとともに、水出口側制御弁14を絞ることに
より油出口3側にも洗浄液を吐出することが容易にでき
、回転体中央部及び油出口側部品も洗浄できる。特に、
スラッジの蓄積しやすい第2図の23の部分を十分に洗
浄するには、洗浄液の流れが必要で、油出口4側に洗浄
液を吐出させることが不可欠である。高流量洗浄では、
前述のごとく、水出口側通路部品、23の部分、回転体
中央部及び油出口側部品を十分洗浄することができるが
、洗浄液は、遠心分離機lを一度通しただけで廃棄する
ことは不経済であるので循環使用する。その結果高流量
洗浄だけで洗浄を行う場合、水出口側通路部品等を洗浄
することにより除去されたスラッジは、洗浄液中に混ざ
り、再び遠心分離機lの原液入口2より遠心分離機lに
供給される。洗浄液は、油出口3側にも吐出されるため
、必然的に分離板21を通過してスラッジが再付着し、
洗浄としては不十分である。Generally, when cleaning sludge adhering to the surface of an object by flowing a cleaning liquid, the higher the flow rate of the cleaning liquid, the better the cleaning effect. In other words, the parts on the water outlet side can be effectively cleaned by high flow rate cleaning, and the cleaning liquid can also be easily discharged to the oil outlet 3 side by throttling the water outlet side control valve 14. Parts on the oil outlet side can also be cleaned. especially,
In order to sufficiently clean the area 23 in FIG. 2 where sludge tends to accumulate, a flow of the cleaning liquid is necessary, and it is essential to discharge the cleaning liquid to the oil outlet 4 side. In high flow cleaning,
As mentioned above, the passage parts on the water outlet side, the part 23, the central part of the rotating body, and the parts on the oil outlet side can be sufficiently cleaned, but the cleaning liquid cannot be discarded after passing through the centrifuge l only once. Since it is economical, use it recyclably. As a result, when cleaning is performed only by high flow rate cleaning, the sludge removed by cleaning the water outlet side passage parts, etc. is mixed into the cleaning liquid and is again supplied to the centrifuge l from the raw solution inlet 2 of the centrifuge l. be done. Since the cleaning liquid is also discharged to the oil outlet 3 side, it inevitably passes through the separation plate 21 and sludge re-adheres.
It is insufficient for cleaning.
そこで、高流量洗浄で分離板21以外の洗浄を行った後
に、スラッジの再付着した分離板21を主として洗浄す
る目的で低流ff1i=&浄に切替える。Therefore, after cleaning the parts other than the separation plate 21 with high flow rate cleaning, the flow rate is switched to low flow rate ff1i=& cleaning mainly for the purpose of cleaning the separation plate 21 on which sludge has reattached.
洗浄液の循環流量を低流量にした場合、前述のごとく、
洗浄液の油出口3側への吐出が止まり、全量水出口4側
へ吐出され、分離板21は浸漬された状態となる。高流
量洗浄により分離板21に再付着したスラッジは、洗浄
液により一度洗われ粘着性のないものであることと洗浄
液の油出口側への流れがないため、遠心力により容易に
外側にふり切られる。従って、低流m洗浄は、分離板2
1のスラッジ洗浄、除去か行えるとともに、水出口通路
側部品の仕上げ洗浄にもなる。As mentioned above, when the circulation flow rate of the cleaning liquid is set to a low flow rate,
Discharge of the cleaning liquid to the oil outlet 3 side is stopped, and the entire amount is discharged to the water outlet 4 side, so that the separation plate 21 is in an immersed state. The sludge that has reattached to the separation plate 21 due to high-flow cleaning is easily shaken off to the outside by centrifugal force because it has been washed once by the cleaning liquid and is non-sticky, and because the cleaning liquid does not flow toward the oil outlet side. . Therefore, the low flow m cleaning is performed by the separation plate 2
In addition to cleaning and removing sludge in step 1, it can also be used as a final cleaning for parts on the water outlet passage side.
このように、高流量洗浄と低流量洗浄を洗浄工程中に切
替えて2段洗浄することにより、回転体内部の全ての部
品を洗浄すことかできるようになり、従来の方法に較べ
洗浄効果を高めることができる。In this way, by switching between high flow rate cleaning and low flow rate cleaning during the cleaning process to perform two-stage cleaning, it is now possible to clean all the parts inside the rotating body, and the cleaning effect is greater than with conventional methods. can be increased.
また、低流量洗浄を高流量洗浄後に行う副効果として、
高流量洗浄により汚れた洗浄液の清浄も同時に行うこと
ができ、洗浄液タンク5に残った洗浄液をろ過等する必
要はなく、新しい液の追加により再使用できる。高流量
洗浄後に、−皮除去されたスラッジを含む洗浄液は、一
部は油出口3側に吐出される。上述のようにその中に含
まれるスラッジは分離板21を通過する間に分離板21
に再付着するが、大部分は水出口4側に吐出される。洗
浄液が高流量のため、その流れに乗って循環する。低流
量洗浄に切替えることにより、スラッジを含む洗浄液は
全て水出口4側に吐出され循環するが、その流量が少な
いため、遠心力によりスラッジは回転体内部のスラッジ
スペース部24に分離蓄積される。スラッジスペース部
24に蓄積されたスラッジは、洗浄工程終了後の排出動
作により、回転体内の洗浄液とともに機外に排出される
。In addition, as a side effect of performing low-flow cleaning after high-flow cleaning,
The dirty cleaning liquid can be cleaned at the same time by high flow rate cleaning, and there is no need to filter the cleaning liquid remaining in the cleaning liquid tank 5, and it can be reused by adding new liquid. After high flow rate cleaning, a part of the cleaning liquid containing the sludge removed is discharged to the oil outlet 3 side. As mentioned above, the sludge contained therein passes through the separation plate 21.
However, most of the water is discharged to the water outlet 4 side. Since the cleaning liquid has a high flow rate, it circulates along with the flow. By switching to low flow rate cleaning, all of the cleaning liquid containing sludge is discharged to the water outlet 4 side and circulated, but since the flow rate is small, the sludge is separated and accumulated in the sludge space 24 inside the rotating body due to centrifugal force. The sludge accumulated in the sludge space portion 24 is discharged to the outside of the machine along with the cleaning liquid inside the rotating body by a discharge operation after the cleaning process is completed.
ハ1発明の効果
この発明は、以上説明したように構成されているので、
以下に記載するような効果を奏する。C1 Effect of the invention Since this invention is configured as explained above,
This produces the effects described below.
即ち、高流量洗浄と低流量洗浄とを組合せることができ
るので、回転体内部の全ての部品を洗浄できるようにな
り、従来の洗浄方法に較べ、洗浄効果を高めることがで
きる。That is, since high flow rate cleaning and low flow rate cleaning can be combined, all parts inside the rotating body can be cleaned, and the cleaning effect can be improved compared to conventional cleaning methods.
高流量洗浄と低流量洗浄の切替えを、洗浄装置の配管の
切替えのみでできるし、また遠心分離機に元々装備して
いるペアリングディスクポンプ20を利用して高流量を
得ることができる。そのため、洗浄装置の送液ポンプ6
は、低流量洗浄用の流量とペアリングディスクポンプの
吐出圧に相当する絞切圧(通常15〜2kg/c/)の
性能を有しておればよい。従って、低容量でコンパクト
且つ低コストの送液ポンプで対応することができるので
、経済的であり、また、技術的に容易な方法で洗浄効果
を高めることができる。Switching between high flow rate cleaning and low flow rate cleaning can be done simply by switching the piping of the cleaning device, and high flow rate can be obtained by using the pairing disk pump 20 originally equipped in the centrifuge. Therefore, the liquid sending pump 6 of the cleaning device
It is sufficient that the pump has the performance of a flow rate for low flow rate cleaning and a throttling pressure (usually 15 to 2 kg/c/) corresponding to the discharge pressure of the pairing disk pump. Therefore, it is possible to use a low-capacity, compact, and low-cost liquid feeding pump, which is economical, and the cleaning effect can be enhanced using a technically easy method.
また、低Zlff量洗浄を高流量洗浄後に行うので、高
流量洗浄により汚れた洗浄液の清浄も同時に行うことが
できる。Further, since the low Zlff amount cleaning is performed after the high flow rate cleaning, cleaning of the cleaning liquid contaminated by the high flow rate cleaning can be performed at the same time.
第1図は従来の遠心分離機の洗浄に用いる装置の系統図
、第2図は遠心分離機の回転体部分の縦断面図、第3図
はこの発明の遠心分離機の洗浄に用いる装置の系統図で
ある。
l 遠心分離機、2 原液入口、3 油出口、4
水出口、5 洗浄液タンク、6送液ポンプ、8
流量調節弁8.14 制御弁、17− 三方制御弁
、20 ペアリングディスクポンプFig. 1 is a system diagram of a conventional device used for cleaning centrifuges, Fig. 2 is a vertical cross-sectional view of the rotating body of a centrifuge, and Fig. 3 is a diagram of a device used for washing centrifuges according to the present invention. It is a system diagram. l Centrifuge, 2 Stock solution inlet, 3 Oil outlet, 4
Water outlet, 5 Cleaning liquid tank, 6 Liquid pump, 8
Flow control valve 8.14 Control valve, 17- Three-way control valve, 20 Pairing disc pump
Claims (1)
心分離機1の原液入口2に注入し、遠心分離機1の油出
口3及び水出口4から吐出される洗浄液を再び洗浄液タ
ンク5に戻す配管系路と、水出口4から吐出される洗浄
液を遠心分離機1内部のペアリングディスクポンプ20
によって直接原液入口2に戻す配管系路とを有する洗浄
装置を用い、水出口4から吐出される洗浄液を直接原液
入口2に戻す高流量洗浄と、遠心分離機1と洗浄液タン
ク5との間に洗浄液を循環させる低流量洗浄とに切替え
る分離板型遠心分離機の洗浄方法。1. Piping for injecting the cleaning liquid from the cleaning liquid tank 5 into the raw liquid inlet 2 of the centrifugal separator 1 using the liquid feed pump 6, and returning the cleaning liquid discharged from the oil outlet 3 and water outlet 4 of the centrifugal separator 1 to the cleaning liquid tank 5 again. A pairing disk pump 20 inside the centrifugal separator 1 transfers the cleaning liquid discharged from the system line and the water outlet 4.
A cleaning device having a piping system that returns the cleaning liquid directly to the raw solution inlet 2 by using a high-flow cleaning method in which the cleaning liquid discharged from the water outlet 4 is returned directly to the raw liquid inlet 2, and between the centrifuge 1 and the cleaning liquid tank 5 A cleaning method for separation plate type centrifugal separators that switches to low-flow cleaning that circulates the cleaning solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32208689A JPH03181348A (en) | 1989-12-12 | 1989-12-12 | Method for cleaning separation plate-type centrifugal separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32208689A JPH03181348A (en) | 1989-12-12 | 1989-12-12 | Method for cleaning separation plate-type centrifugal separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03181348A true JPH03181348A (en) | 1991-08-07 |
Family
ID=18139759
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP32208689A Pending JPH03181348A (en) | 1989-12-12 | 1989-12-12 | Method for cleaning separation plate-type centrifugal separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03181348A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1712289A1 (en) * | 2005-04-14 | 2006-10-18 | Nuova Maip Macchine Agricole Industriali Pieralisi S.p.A. | Washing method for centrifugal separators of mixtures composed of two liquid phases and solid and non-solid sediments |
| JP2014205132A (en) * | 2013-04-15 | 2014-10-30 | シンフン プレシジョン カンパニー リミテッド | Centrifugal circulation purifier system |
-
1989
- 1989-12-12 JP JP32208689A patent/JPH03181348A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1712289A1 (en) * | 2005-04-14 | 2006-10-18 | Nuova Maip Macchine Agricole Industriali Pieralisi S.p.A. | Washing method for centrifugal separators of mixtures composed of two liquid phases and solid and non-solid sediments |
| AU2006201400B2 (en) * | 2005-04-14 | 2010-04-29 | Nuova Maip Macchine Agricole Industriali Pieralisi S.P.A. | Washing method for centrifugal separators of mixtures composed of two liquid phases and solid and non-solid sediments |
| JP2014205132A (en) * | 2013-04-15 | 2014-10-30 | シンフン プレシジョン カンパニー リミテッド | Centrifugal circulation purifier system |
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