JP2003320371A - Apparatus for cleaning and recovering coolant - Google Patents

Apparatus for cleaning and recovering coolant

Info

Publication number
JP2003320371A
JP2003320371A JP2002131487A JP2002131487A JP2003320371A JP 2003320371 A JP2003320371 A JP 2003320371A JP 2002131487 A JP2002131487 A JP 2002131487A JP 2002131487 A JP2002131487 A JP 2002131487A JP 2003320371 A JP2003320371 A JP 2003320371A
Authority
JP
Japan
Prior art keywords
coolant
liquid
tank
oil
layer
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
JP2002131487A
Other languages
Japanese (ja)
Inventor
Tadashi Toyama
直史 外山
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.)
MEKKU CORP KK
Original Assignee
MEKKU CORP KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by MEKKU CORP KK filed Critical MEKKU CORP KK
Priority to JP2002131487A priority Critical patent/JP2003320371A/en
Publication of JP2003320371A publication Critical patent/JP2003320371A/en
Pending legal-status Critical Current

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Landscapes

  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Removal Of Floating Material (AREA)
  • Auxiliary Devices For Machine Tools (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus which eliminates foul odor in a coolant discharge vessel in such a way that oil floating on the surface of a coolant in the vessel is separated and recovered, and that the coolant is refluxed after aerobic and anaerobic bacteria propagating in the vessel are killed. <P>SOLUTION: The apparatus is constituted of a processing tank 9 with a built-in heater provided with a level gauge having a first and a second electrodes L1, L2 detecting an aqueous liquid layer 13 and an oil layer 14, and with an automatic relief valve FV; a coolant returning pipe 17 continuously feeding the upper layer liquid and the floating oil in the coolant discharge vessel 1 to the processing tank 9 and having a vertical part 19 and a horizontal part 20 for holding a liquid to be treated in the processing tank for a specified time; and a floating oil recovery pipe 21 which is opened at and connected to a position lower than the horizontal part of a returning pipe 17 and between the first and the second electrodes, and having an electromagnetic valve 22 which is opened for a specified period of time by an oil-layer detecting signal from the second electrode. <P>COPYRIGHT: (C)2004,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明が属する技術分野】この発明は、受容タンクに収
容されているクーラント液の浮上油を分離し、腐敗や悪
臭を防止する浄化回収装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a purification / recovery device for separating floating oil of a coolant contained in a receiving tank to prevent spoilage and bad odor.

【0002】[0002]

【従来の技術】機械加工工場の研削機や切削機の冷却液
(クーラント)に混入した機械油などがクーラント排液
貯槽内で油膜となって液面を覆うことからクーラントが
腐敗し悪臭を発生することが知られている。即ち、貯槽
内のクーラント液は、好気性菌によって液中酸素を消費
され、次いで嫌気性菌(硫酸塩還元菌)が繁殖すること
によって悪臭が発生する。クーラント液の悪臭・腐敗を
防止する装置としてベルトによって浮上油を吸着除去す
る装置、空気曝気、フィルターろ過と比重差による分離
や中空糸膜ろ過などの方式が使用されているが、いずれ
も所期の目的を達していない。
2. Description of the Related Art Machine oil mixed in the coolant (coolant) of a grinding machine or a cutting machine in a machining factory forms an oil film in the coolant drainage storage tank to cover the liquid surface, causing the coolant to spoil and produce a foul odor. Is known to do. That is, the liquid coolant in the storage tank consumes oxygen in the liquid by aerobic bacteria, and then anaerobic bacteria (sulfate-reducing bacteria) propagate, thereby causing a bad odor. As a device to prevent the bad odor and spoilage of the coolant, a device that adsorbs and removes floating oil by a belt, air aeration, filter filtration and separation by specific gravity difference, hollow fiber membrane filtration, etc. are used. Has not reached its purpose.

【0003】[0003]

【発明が解決しようとする課題】本発明は、浮上油を比
重分離する過程で加熱することによって液中の好気性菌
と嫌気性菌を殺菌してクーラント液を回収する装置を提
供するものである。更に、処理タンクに供給される被処
理クーラントと浮上油を分離除去した加熱殺菌クーラン
トを熱交換させることによってエネルギーコストを低減
できる装置を提供するものである。
DISCLOSURE OF THE INVENTION The present invention provides an apparatus for recovering a coolant liquid by heating floating oil in the process of specific gravity separation to sterilize aerobic bacteria and anaerobic bacteria in the liquid and recover the coolant liquid. is there. Further, the present invention provides an apparatus capable of reducing energy cost by heat-exchanging a heat-sterilized coolant from which floating oil is separated and removed from a coolant to be treated supplied to a treatment tank.

【0004】[0004]

【課題を解決するための手段】本発明装置は、工作機械
などからのクーラント排液を貯留する排液槽と、水液層
と油層レベルを検知する第1、第2の電極を有するレベ
ル計とタンク内の所定水位で閉止する外気開放弁を備え
てヒータを内蔵した処理タンクと、前記クーラント排液
槽内の上層液を浮上油と共に吸引するポンプに接続し前
記処理タンク上部に開口する被処理液供給管と、前記処
理タンク内の下部に開口し、該タンク内において被処理
液を所定時間滞留させるための高さを有する垂直部と水
平部を有して前記クーラント排液槽に連絡するクーラン
ト戻し管と、前記戻し管水平部より下方で且つ前記レベ
ル計の第1電極と第2電極との間に開口し第2電極から
の油層検知信号によって作動する電磁弁を備えた浮上油
回収管とから構成され、処理タンク内の液温を所定温度
に維持して排液槽内の好気性菌と嫌気性菌を殺菌して排
液槽に自然落下方式で戻すことによって排液槽から発生
する悪臭を防止すると共に浮上油を自動的に回収するも
のである。加熱温度は通常70〜90℃の範囲で充分で
あり、内容積1000Lまでの排液槽であれば数10時
間の運転で効果がある。本発明装置は、自然滴下方式で
回収クーラントを戻すので動力費が少ない利点がある
が、供給管とクーラント戻し管を熱交換器を介して接続
することにより更にエネルギーコストを低減できる。
The device of the present invention is a level meter having a drainage tank for storing a coolant drainage from a machine tool or the like, and first and second electrodes for detecting a water liquid layer and an oil layer level. And a processing tank with a built-in heater equipped with an outside air release valve that closes at a predetermined water level in the tank, and a pump that is connected to a pump that sucks the upper layer liquid in the coolant drainage tank together with the floating oil and that opens above the processing tank. A processing liquid supply pipe and a vertical portion and a horizontal portion, which are opened at a lower portion in the processing tank and have a height for allowing the liquid to be treated to stay in the tank for a predetermined time, are connected to the coolant drainage tank. Floating oil provided with a coolant return pipe and a solenoid valve which is opened below the horizontal part of the return pipe and between the first electrode and the second electrode of the level meter and which is operated by an oil layer detection signal from the second electrode. Composed of a collection pipe By maintaining the liquid temperature in the treatment tank at a predetermined temperature and sterilizing aerobic and anaerobic bacteria in the drainage tank and returning it to the drainage tank by the natural fall method, the bad odor generated from the drainage tank is eliminated. This is to prevent and automatically collect the floating oil. A heating temperature of 70 to 90 ° C. is usually sufficient, and a drainage tank having an internal volume of up to 1000 L is effective for several tens hours of operation. The device of the present invention has an advantage of low power cost because the recovered coolant is returned by the natural dropping method, but the energy cost can be further reduced by connecting the supply pipe and the coolant return pipe through the heat exchanger.

【0005】[0005]

【発明の実施の形態】図1は、装置の熱効率を向上させ
るため熱交換器を設けた場合である。1は工作機械など
に付設されている使用済みクーラント排液槽、2はクー
ラント液層、3は上層液、4は浮上油、5は液面に浮い
た吸い込みフロート、6は吸い込みホース、7は吸引ポ
ンプ、8はポンプに接続している供給管であって処理タ
ンク9の上部10に開口している。11は槽内温度を7
0℃以上に加熱保持するヒータ、LGは電極式レベル計
であってアース電極L0、第1電極L1、第2電極L2
を備えている。FVはフロート式外気開放弁であってタ
ンク内の運転水位16以上で作動し、タンク内を外気と
遮断する。12はドレン弁である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows a case where a heat exchanger is provided to improve the thermal efficiency of the apparatus. 1 is a used coolant drainage tank attached to a machine tool or the like, 2 is a coolant liquid layer, 3 is an upper layer liquid, 4 is floating oil, 5 is a suction float floating on the liquid surface, 6 is a suction hose, and 7 is A suction pump, 8 is a supply pipe connected to the pump and opens at an upper portion 10 of the processing tank 9. 11 is the temperature inside the tank 7
A heater for heating and holding at 0 ° C. or more, LG is an electrode type level meter, and is an earth electrode L0, a first electrode L1, a second electrode L2.
Is equipped with. The FV is a float type outside air release valve that operates at an operating water level of 16 or higher in the tank and shuts off the inside of the tank from the outside air. 12 is a drain valve.

【0006】13はタンク内の液層、14は油層、15
は界面、16は液面である。17は戻し管であって、下
端18がタンク下部に開口し所定高さの垂直部19と水
平部20を備え、熱交換器Hを経て排液槽1に連絡す
る。水平部の高さ即ち、垂直部の長さは被処理液をタン
ク内に充分な時間滞留させると共に運転中の戻し液面1
6を規定する。即ち、液面が水平部に至れば戻し液が流
れ、低くなれば戻し液は流出しなくなる。21は浮上油
回収管であって、第1電極と第2電極間の油層14に連
通する位置に開口接続21aされ、電磁弁22はレベル
計の第2電極L2の出力によって開弁し所定時間後に閉
弁する。23は浮上油回収槽である。
13 is a liquid layer in the tank, 14 is an oil layer, 15
Is an interface and 16 is a liquid surface. Reference numeral 17 denotes a return pipe, the lower end 18 of which is opened at the lower part of the tank and has a vertical portion 19 and a horizontal portion 20 each having a predetermined height, and communicates with the drainage tank 1 via the heat exchanger H. The height of the horizontal part, that is, the length of the vertical part is such that the liquid to be treated is retained in the tank for a sufficient time and the level of the returning liquid 1 during operation
6 is defined. That is, the return liquid flows when the liquid level reaches the horizontal portion, and the return liquid does not flow out when the liquid level becomes low. Reference numeral 21 denotes a floating oil recovery pipe, which is opened and connected 21a at a position communicating with the oil layer 14 between the first electrode and the second electrode, and the solenoid valve 22 is opened by the output of the second electrode L2 of the level meter for a predetermined time. It will be closed later. 23 is a floating oil recovery tank.

【0007】[0007]

【実施例】切削加工機からのクーラント排液(19〜2
2℃)槽(容量300L)から排液を10L/1時間で
加工機運転中、連続して空の処理タンク(有効容積7
L)内に供給した。図2の水位Dでヒータが通電し、約
40分後に設定温度80℃になり、水面16がA位置に
なってフロート弁FVが作動してタンク内が密閉され
た。初期の状態では浮上油とクーラント液は層状に分離
していないが、戻し管からのクーラント液が戻されてい
る間に次第に分離して油層14の厚さが増し、界面がB
からC以下になると第1電極は液層を検知し、第2電極
は油層を検知しているのでこの差信号によって電磁弁2
2が作動して浮上油が排出された。約2分後に電磁弁2
2が自動的に閉弁する。液面Aの低下によってフロート
弁FVが開いてタンク内が大気圧となる。液面Aが、戻
し管水平部20より低い位置になっているから戻しクー
ラントは流れ出ないが、クーラント排液は連続供給され
ているから液面は再び上昇し上記動作を繰り返す。
[Example] Coolant drainage from a cutting machine (19-2
2 ℃) Drainage from the tank (capacity 300 L) at 10 L / 1 hour while the processing machine is operating, continuously empty processing tank (effective volume 7
L). The heater was energized at the water level D in FIG. 2, the temperature reached 80 ° C. after about 40 minutes, the water surface 16 was moved to the A position, and the float valve FV was activated to seal the inside of the tank. In the initial state, the floating oil and the coolant liquid are not separated in layers, but while the coolant liquid from the return pipe is being returned, they are gradually separated and the thickness of the oil layer 14 increases, and the interface B
From C to C or less, the first electrode detects the liquid layer and the second electrode detects the oil layer.
2 was activated and the floating oil was discharged. Solenoid valve 2 after about 2 minutes
2 automatically closes. The float valve FV opens due to the decrease in the liquid level A, and the inside of the tank becomes atmospheric pressure. The return coolant does not flow out because the liquid level A is lower than the horizontal position of the return pipe 20, but the coolant drainage is continuously supplied, so the liquid level rises again and the above operation is repeated.

【0008】1日6時間運転(60L処理)を5日間継
続した。10時間後、0.5Lの浮上油が回収され、3
日目にはクーラント排液槽表面の浮上油膜が視認されな
くなり、腐敗臭も少なくなった。5日(30時間)後、
腐敗臭はほぼ完全に除去された。この間、処理タンクの
温度は80度に維持され、熱交換器(6000Kca
l)からの供給液温度60℃、排液槽1への戻し液温度
は40℃に維持されていた。
Operation for 6 hours a day (60 L treatment) was continued for 5 days. After 10 hours, 0.5 L of floating oil was collected and 3
On the day, the floating oil film on the surface of the coolant drainage tank was no longer visible and the rotting odor was reduced. After 5 days (30 hours),
The rotten odor was almost completely removed. During this time, the temperature of the processing tank was maintained at 80 degrees, and the heat exchanger (6000 Kca
The temperature of the supply liquid from 1) was maintained at 60 ° C, and the temperature of the liquid returned to the drainage tank 1 was maintained at 40 ° C.

【0009】上記実施例における処理前液(液温20
℃)と運転1時間30分後の処理液(液温32℃)につ
いて上水試験法(2001)VIII−4、3、2によ
り硫酸塩還元菌を測定した結果、処理前液は2.4×1
MPN/100mLであったが、処理液は1.7×
10MPN/100mLであった。
Pretreatment liquid (liquid temperature 20
C.) and a treatment liquid (liquid temperature 32.degree. C.) after 1 hour and 30 minutes of operation, the sulfate-reducing bacteria were measured by the clean water test method (2001) VIII-4, 3 and 2, and the pretreatment liquid was 2.4. × 1
0 8 MPN / 100 mL at which was, a processing liquid 1.7 ×
It was 10 5 MPN / 100 mL.

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

【図1】装置の全体構成図FIG. 1 is an overall configuration diagram of the device

【図2】液面変化を示す要部構成図FIG. 2 is a configuration diagram of a main part showing a liquid level change.

【符号の説明】[Explanation of symbols]

1 クーラント排液槽 2 クーラント液層 3 上層液 4 浮上油 5 吸い込みフロート 6 ホース 7 吸引ポンプ 8 供給管 9 処理タンク 10 タンク上部 11 ヒータ 12 ドレン弁 LG レベル計 L0、L1、L2 電極 FV フロート式空気弁 13 液層 14 油層 15 界面 16 液面 A、B、C、D 変動液面 17 戻し管 18 下端 19 垂直部 20 水平部 21 浮上油回収管 22 電磁弁 1 Coolant drainage tank 2 Coolant liquid layer 3 Upper layer liquid 4 floating oil 5 suction float 6 hose 7 suction pump 8 supply pipes 9 Processing tank 10 Tank top 11 heater 12 drain valve LG level meter L0, L1, L2 electrodes FV float type air valve 13 liquid layers 14 oil layer 15 Interface 16 Liquid level A, B, C, D Fluctuating liquid level 17 Return tube 18 bottom 19 Vertical part 20 Horizontal part 21 Floating oil recovery pipe 22 Solenoid valve

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】クーラント排液槽と、水液層と油層レベル
を検知する第1、第2の電極を有するレベル計と所定水
位で閉止する外気開放弁を備えたヒータ内蔵処理タンク
と、前記クーラント排液槽内の上層液を浮上油と共に吸
引するポンプに接続し前記処理タンク上部に開口する被
処理液供給管と、前記処理タンク内の下部に開口し、該
タンク内において被処理液を所定時間滞留させるための
高さを有する垂直部と水平部を有して前記クーラント排
液槽に連絡するクーラント戻し管と、前記戻し管水平部
より下方で且つ前記レベル計の第1電極と第2電極との
間に開口し第2電極からの油層検知信号によって作動す
る電磁弁を備えた浮上油回収管とからなるクーラント液
浄化回収装置。
1. A processing tank with a built-in heater, comprising a coolant drainage tank, a level meter having first and second electrodes for detecting a water liquid layer and an oil layer level, and an outside air release valve for closing at a predetermined water level, A liquid to be treated supply pipe which is connected to a pump for sucking the upper layer liquid in the coolant drainage tank together with the floating oil and which is opened to the upper part of the treatment tank, and which is opened to the lower part in the treatment tank to store the liquid to be treated in the tank A coolant return pipe having a vertical portion and a horizontal portion having a height for retaining for a predetermined time and communicating with the coolant drainage tank, a first electrode of the level meter and a first electrode of the level meter which are below the return pipe horizontal portion. A coolant liquid purification and recovery device comprising a floating oil recovery pipe provided with a solenoid valve which is opened between the two electrodes and which is activated by an oil layer detection signal from the second electrode.
【請求項2】供給管とクーラント戻し管が熱交換器を通
る請求項1記載のクーラント液浄化回収装置。
2. The coolant liquid purifying and collecting apparatus according to claim 1, wherein the supply pipe and the coolant return pipe pass through the heat exchanger.
【請求項3】処理タンク内の液温を75〜90℃の範囲
に維持することを特徴とする請求項1又は2記載のクー
ラント液浄化回収装置。
3. The coolant liquid purifying and recovering apparatus according to claim 1 or 2, wherein the liquid temperature in the processing tank is maintained in the range of 75 to 90 ° C.
JP2002131487A 2002-05-07 2002-05-07 Apparatus for cleaning and recovering coolant Pending JP2003320371A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002131487A JP2003320371A (en) 2002-05-07 2002-05-07 Apparatus for cleaning and recovering coolant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002131487A JP2003320371A (en) 2002-05-07 2002-05-07 Apparatus for cleaning and recovering coolant

Publications (1)

Publication Number Publication Date
JP2003320371A true JP2003320371A (en) 2003-11-11

Family

ID=29544103

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002131487A Pending JP2003320371A (en) 2002-05-07 2002-05-07 Apparatus for cleaning and recovering coolant

Country Status (1)

Country Link
JP (1) JP2003320371A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104608005A (en) * 2015-02-03 2015-05-13 励志辉 Cutting fluid circulating system
CN112123009A (en) * 2020-08-24 2020-12-25 北京现代汽车有限公司 Sump oil collecting system
CN113211536A (en) * 2021-05-20 2021-08-06 安吉兴华电力管道股份有限公司 PVC pipe production cutting equipment with dust removal function

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104608005A (en) * 2015-02-03 2015-05-13 励志辉 Cutting fluid circulating system
CN112123009A (en) * 2020-08-24 2020-12-25 北京现代汽车有限公司 Sump oil collecting system
CN113211536A (en) * 2021-05-20 2021-08-06 安吉兴华电力管道股份有限公司 PVC pipe production cutting equipment with dust removal function

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