JP3148578U - Vacuum processing equipment for emulsified waste liquid - Google Patents

Vacuum processing equipment for emulsified waste liquid Download PDF

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JP3148578U
JP3148578U JP2008008576U JP2008008576U JP3148578U JP 3148578 U JP3148578 U JP 3148578U JP 2008008576 U JP2008008576 U JP 2008008576U JP 2008008576 U JP2008008576 U JP 2008008576U JP 3148578 U JP3148578 U JP 3148578U
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vacuum
waste liquid
chamber
emulsified waste
emulsified
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勝 小野田
勝 小野田
伸幸 真鍋
伸幸 真鍋
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協和船舶工業株式会社
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Abstract

【課題】大量の廃液でも迅速に効率よく、しかも安価に処理することができる乳化廃液の真空式処理装置を提供する。【解決手段】内部が真空減圧状態に保たれ真空減圧室を有し、真空減圧室内に乳化廃液を噴霧または薄膜にして分散装置に分散する微粒霧化装置を備え、下部に乳化廃液を貯留する貯留槽を有する真空減圧装置と、微粒霧化装置に乳化廃液を圧送状態で供給する手段と、真空減圧室内で蒸発した水蒸気を取り出す蒸気ダクトと、蒸気ダクトを通じて真空減圧室に連通し、真空減圧室を真空減圧状態に保つ真空減圧手段を有すると共に、蒸気ダクトから流入する水蒸気を冷却して液化する液化装置と、真空減圧装置から水分を除去された廃液を排出する手段と、から構成される。【選択図】 図1Disclosed is a vacuum processing apparatus for emulsified waste liquid, which can process a large amount of waste liquid quickly, efficiently and inexpensively. An inside of the vacuum decompression chamber has a vacuum decompression chamber, a fine atomization device for spraying or thinning the emulsified waste liquid into a dispersion device, and dispersing the emulsified waste liquid in a lower portion. Vacuum depressurization device having a storage tank, means for supplying emulsified waste liquid to the atomizing device in a pumped state, a steam duct for taking out water vapor evaporated in the vacuum depressurization chamber, a vacuum duct communicating with the vacuum depressurization chamber through the steam duct, and vacuum depressurization A vacuum depressurizing means for maintaining the chamber in a vacuum depressurized state, a liquefying device for cooling and liquefying the water vapor flowing from the steam duct, and a means for discharging the waste liquid from which moisture has been removed from the vacuum depressurizing device. . [Selection] Figure 1

Description

本考案は、例えば、船舶機関あるいは発電所の機関などで使用される潤滑油などに水分が乳化状態で分散され劣化した乳化廃液から水分を分離して潤滑油などを再生するための、乳化廃液の真空式処理装置に関するものである。   The present invention, for example, emulsified waste liquid for separating the moisture from the emulsified waste liquid that has been dispersed and deteriorated in the lubricating oil used in ship engines or power plant engines, etc. to regenerate the lubricant This relates to a vacuum processing apparatus.

従来の乳化廃液の処理装置としては、長時間をかけて油水分離を行うか、電気化学的に処理する方法があった。   As a conventional emulsification waste liquid treatment apparatus, there is a method in which oil-water separation is performed over a long period of time or an electrochemical treatment is performed.

しかしながら、上記従来の方法では、水分が油分に微細粒化状態で電気的に安定して分散した、いわゆる乳化状態での水分の分離処理は、分離能力に限界があるだけでなく、時間とコストがかかりその実用化が極めて困難であった。   However, in the conventional method described above, the water separation process in the so-called emulsified state in which the water is electrically stably dispersed in the oil in a finely divided state has not only limited separation ability but also time and cost. It was extremely difficult to put it into practical use.

本考案が解決しようとする課題は、大量の廃液でも迅速に効率よく、しかも安価に処理することができる乳化廃液の真空式処理装置を提供することにある。   The problem to be solved by the present invention is to provide a vacuum processing apparatus for emulsified waste liquid that can be processed quickly, efficiently and inexpensively even with a large amount of waste liquid.

本考案の乳化廃液の真空式処理装置は、内部が真空減圧状態に保たれ真空減圧室を有し、該真空減圧室内に乳化廃液を噴霧または薄膜にして分散装置に分散する微粒霧化装置を備え、下部に乳化廃液を貯留する貯留槽を有する真空減圧装置と、上記微粒霧化装置に乳化廃液を圧送状態で供給する手段と、上記真空減圧室内で蒸発した水蒸気を取り出す蒸気ダクトと、該蒸気ダクトを通じて上記真空減圧室に連通し、該真空減圧室を真空減圧状態に保つ真空減圧手段を有すると共に、上記蒸気ダクトから流入する水蒸気を冷却して液化する液化装置と、上記真空減圧装置から水分を除去された廃液を排出する手段と、から構成されることを特徴とする。   The vacuum processing apparatus for emulsified waste liquid according to the present invention comprises a fine atomization apparatus that has a vacuum decompression chamber with the inside kept in a vacuum decompression state, and sprays or thinly disperses the emulsification waste liquid in the vacuum decompression chamber. A vacuum decompression device having a storage tank for storing the emulsified waste liquid at the bottom, means for supplying the emulsified waste liquid to the fine atomizer in a pumped state, a steam duct for taking out water vapor evaporated in the vacuum decompression chamber, A vacuum depressurization means that communicates with the vacuum depressurization chamber through a steam duct and maintains the vacuum depressurization chamber in a vacuum depressurization state; a liquefaction device that cools and liquefies water vapor flowing from the steam duct; and the vacuum depressurization device And a means for discharging the waste liquid from which moisture has been removed.

本考案の乳化廃液の真空式処理装置は、基本的に水と油の蒸気圧差を利用して、比較的に低い温度でも効率よく水を廃油から分離することができるという利点がある。また、低温で処理できるため、排熱または処理液に蓄積された熱を利用することができて、新たな熱源を必要としないことで環境に優しい処理となる。   The vacuum processing apparatus for emulsified waste liquid according to the present invention has an advantage that water can be efficiently separated from waste oil even at a relatively low temperature by basically utilizing the vapor pressure difference between water and oil. Moreover, since it can process at low temperature, waste heat or the heat | fever accumulate | stored in the process liquid can be utilized, and it becomes an environmentally friendly process by not requiring a new heat source.

図1は、本考案装置の1実施例の説明図であって、1は原液槽、2は真空減圧装置、3は供給パイプ、4は自給/強制切換弁、4aは供給ポンプ、5は微粒霧化装置、6は分散装置、7は加熱板、8は液面調整堰、9は排出パイプ、10は蒸気ダクト、11は液化装置、12は冷却器、13は真空ポンプ、14は排水パイプ、15はエンジン、16は軸受、17はクーラー、18はフィルターである。   FIG. 1 is an explanatory view of an embodiment of the device of the present invention, wherein 1 is a stock solution tank, 2 is a vacuum decompression device, 3 is a supply pipe, 4 is a self-feed / forced switching valve, 4a is a supply pump, and 5 is a fine particle. An atomizer, 6 is a dispersing device, 7 is a heating plate, 8 is a liquid level adjusting weir, 9 is a discharge pipe, 10 is a steam duct, 11 is a liquefier, 12 is a cooler, 13 is a vacuum pump, and 14 is a drain pipe. , 15 is an engine, 16 is a bearing, 17 is a cooler, and 18 is a filter.

上記原液槽1には乳化廃液(廃油と水とその他のスラッジ等の固形分のエマルジョン)が貯留され、必要に応じて上記真空減圧装置2の貯留槽2a内に供給される。該貯留槽2a内に供給される乳化廃液は、供給コントローラ2bによりその供給量が適宜調整される。エンジン15の運転中は、パイプ7a、7bにより乳化廃液を加熱板7に送って、該加熱板7を加熱し、分散装置6上の薄膜に蒸発熱を補助的に付与して、蒸発を促進させる。   The stock solution tank 1 stores an emulsified waste liquid (emulsion of waste oil, water, and other solids such as sludge), and is supplied into the storage tank 2a of the vacuum decompression device 2 as necessary. The supply amount of the emulsified waste liquid supplied into the storage tank 2a is appropriately adjusted by the supply controller 2b. During operation of the engine 15, the emulsified waste liquid is sent to the heating plate 7 through the pipes 7 a and 7 b, the heating plate 7 is heated, and the evaporation heat is supplementarily applied to the thin film on the dispersion device 6 to promote evaporation. Let

上記貯留槽2a内の乳化廃液は、供給パイプ3を通じて微粒霧化装置5に送られる。該供給パイプ3の途中には、上記供給ポンプ4aが設けられ、乳化廃液を上記微粒霧化装置5に圧送するようになっている。   The emulsified waste liquid in the storage tank 2 a is sent to the atomizing device 5 through the supply pipe 3. In the middle of the supply pipe 3, the supply pump 4 a is provided, and the emulsified waste liquid is pumped to the fine atomizer 5.

上記微粒霧化装置5からは乳化廃液が微粒状で真空減圧室2c内に噴霧され、分散装置6上に降下して薄い膜になる。該真空減圧室2c内は上記蒸気ダクト10および液化装置11を通じて、上記真空ポンプ13により減圧状態(例えば、−0.6気圧)に置かれるので、噴霧された乳化廃液のうち水分および一部の油分は、落下中に或いは分散装置6上の膜状態から蒸発し、上記蒸気ダクト10に送られる。この蒸発は、真空減圧室2cの真空度や廃液の温度により生じるので、比較的に低い温度でも、真空に近い減圧状態であれば、蒸発し易い。   From the fine atomizing device 5, the emulsified waste liquid is fine and sprayed into the vacuum decompression chamber 2c and descends onto the dispersing device 6 to form a thin film. The vacuum decompression chamber 2c is placed in a decompressed state (for example, -0.6 atm) by the vacuum pump 13 through the steam duct 10 and the liquefying device 11, so that moisture and a part of the sprayed emulsified waste liquid are contained. The oil is evaporated from the film state on the dispersing device 6 during the fall or sent to the steam duct 10. Since this evaporation occurs depending on the degree of vacuum in the vacuum decompression chamber 2c and the temperature of the waste liquid, it is easy to evaporate even at a relatively low temperature in a decompressed state close to vacuum.

蒸発しない廃液は、上記分散装置6から加熱板7上に降下および流下し、上記貯留槽2aに戻され再循環される。貯留槽2a内の液は、一定の液面高さを超えると、液面調整堰8から排出槽2dに溢流し、排出パイプ9から外部に排出される。この排出液(水分が除かれた廃液)は、従来公知の分離技術によりスラッジ等の固形分を取り除かれ、再生油となる。   Waste liquid that does not evaporate descends and flows from the dispersing device 6 onto the heating plate 7 and is returned to the storage tank 2a for recirculation. When the liquid in the storage tank 2a exceeds a certain liquid level, it overflows from the liquid level adjusting weir 8 to the discharge tank 2d and is discharged from the discharge pipe 9 to the outside. This discharged liquid (waste liquid from which moisture has been removed) is removed from solids such as sludge by a conventionally known separation technique, and becomes regenerated oil.

上記蒸気ダクト10内は上記液化装置11に近づくにしたがって低温となる。特に、蒸気ダクト10側の上昇区域10aにおいては、蒸気状態の水分(水蒸気)および一部の油分のうち、油分が液化し、該上昇区域10aの蒸気ダクト10の傾斜に沿って逆流し、上記真空減圧室2c内に戻る。   The inside of the steam duct 10 becomes lower in temperature as it approaches the liquefying device 11. In particular, in the rising area 10a on the steam duct 10 side, the oil component is liquefied out of the moisture (water vapor) and some oil components in the vapor state, and flows backward along the inclination of the steam duct 10 in the rising area 10a. Return to the vacuum decompression chamber 2c.

油分が除去された水蒸気は、上記蒸気ダクト10を通って、液化装置11に入り、ここで冷却されて水になり、排水パイプ14から排出される。冷却器12には冷却水が循環し、液化装置11内を冷却する。   The steam from which the oil has been removed passes through the steam duct 10 and enters the liquefaction device 11 where it is cooled to water and discharged from the drain pipe 14. Cooling water circulates in the cooler 12 to cool the inside of the liquefying device 11.

本考案装置の1実施例を示す説明図である。It is explanatory drawing which shows one Example of this invention apparatus.

符号の説明Explanation of symbols

1 原液槽
2 真空減圧装置
2a 貯留槽
2b 供給コントローラ
2c 真空減圧室
2d 排出槽
3 供給パイプ
4 自給/強制切換弁
4a 供給ポンプ
5 微粒霧化装置
6 分散装置
7 加熱板
8 液面調整堰
9 排出パイプ
10 蒸気ダクト
10a 上昇区域
11 液化装置
12 冷却器
13 真空ポンプ
14 排水パイプ
15 エンジン
16 軸受
17 クーラー
18 フィルター
DESCRIPTION OF SYMBOLS 1 Stock solution tank 2 Vacuum decompression device 2a Storage tank 2b Supply controller 2c Vacuum decompression chamber 2d Discharge tank 3 Supply pipe 4 Self-supply / forced switching valve 4a Supply pump 5 Atomizer 6 Dispersing device 7 Heating plate 8 Liquid level adjustment weir 9 Discharge Pipe 10 Steam duct 10a Ascending zone 11 Liquefaction device 12 Cooler 13 Vacuum pump 14 Drain pipe 15 Engine 16 Bearing 17 Cooler 18 Filter

Claims (1)

内部が真空減圧状態に保たれ真空減圧室を有し、該真空減圧室内に乳化廃液を噴霧または薄膜にして分散装置に分散する微粒霧化装置を備え、下部に乳化廃液を貯留する貯留槽を有する真空減圧装置と、上記微粒霧化装置に乳化廃液を圧送状態で供給する手段と、上記真空減圧室内で蒸発した水蒸気を取り出す蒸気ダクトと、該蒸気ダクトを通じて上記真空減圧室に連通し、該真空減圧室を真空減圧状態に保つ真空減圧手段を有すると共に、上記蒸気ダクトから流入する水蒸気を冷却して液化する液化装置と、上記真空減圧装置から水分を除去された廃液を排出する手段と、から構成されることを特徴とする乳化廃液の真空式処理装置。 The inside of the vacuum decompression chamber has a vacuum decompression chamber, and is equipped with a fine-grain atomizing device that sprays or thinly disperses the emulsified waste liquid into the dispersion device, and a storage tank for storing the emulsified waste liquid at the bottom. A vacuum depressurizing device, means for supplying the emulsified waste liquid to the atomizing device in a pumped state, a steam duct for taking out water vapor evaporated in the vacuum depressurizing chamber, and the vacuum depressurizing chamber through the steam duct, A vacuum depressurization means for keeping the vacuum depressurization chamber in a vacuum depressurized state, a liquefying device for cooling and liquefying the water vapor flowing from the steam duct, and a means for discharging the waste liquid from which moisture has been removed from the vacuum depressurization device; A vacuum processing apparatus for an emulsified waste liquid.
JP2008008576U 2008-12-08 2008-12-08 Vacuum processing equipment for emulsified waste liquid Expired - Lifetime JP3148578U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102430252A (en) * 2011-09-21 2012-05-02 重庆工商大学 Double-effect heat transfer falling film vacuum oil-water separating device
JP2014028362A (en) * 2012-06-25 2014-02-13 Kyowa Senpaku Kogyo Kk Device and method for recycling emulsified waste oil

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102430252A (en) * 2011-09-21 2012-05-02 重庆工商大学 Double-effect heat transfer falling film vacuum oil-water separating device
JP2014028362A (en) * 2012-06-25 2014-02-13 Kyowa Senpaku Kogyo Kk Device and method for recycling emulsified waste oil

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