JPH10202007A - Oil separation of kitchen waste water and device therefor - Google Patents
Oil separation of kitchen waste water and device thereforInfo
- Publication number
- JPH10202007A JPH10202007A JP9027268A JP2726897A JPH10202007A JP H10202007 A JPH10202007 A JP H10202007A JP 9027268 A JP9027268 A JP 9027268A JP 2726897 A JP2726897 A JP 2726897A JP H10202007 A JPH10202007 A JP H10202007A
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- Prior art keywords
- oil
- electrolytic
- electrolysis
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Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、レストランや食堂
等からの乳化された油脂分を含む厨房排水を電気分解に
より油脂分を分離除去するとともに、腐敗防止、殺菌、
消臭する方法と装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for separating and removing fats and oils from kitchen wastewater containing emulsified fats and oils from restaurants and cafeterias by electrolysis, as well as for preventing decay and sterilizing.
The present invention relates to a deodorizing method and apparatus.
【0002】[0002]
【従来の技術】従来、レストランや食堂等からの油分を
含む厨房排水は、例えばグリーストラップなどをもちい
て油分と水との比重差による浮上分離を利用して油分除
去させ処理水を流出させている。近年、レストランや食
堂等においては、省力化のために食器等の機械的洗浄が
多用され、界面活性剤を用い、機械的撹拌作用を与えて
食器等を洗浄しているので、上記排水の油分等の汚れを
取込んだ上記界面活性剤の分子の集合体であるミセルに
よって高度の乳化を形成することとなる。界面活性剤を
用いて洗浄した場合、上記界面活性剤を排水中で表面は
負(マイナス)に荷電しており同種イオンの反撥力によ
り安定化した乳化を形成させている。一方、マイナスに
荷電している上記汚れのミセルにカチオン性界面活性剤
の水溶液を添加させることにより、電気的に中和して上
記ミセルを破壊させて、上記油分を顕在化させ浮上分離
により油分除去させることができる。2. Description of the Related Art Conventionally, kitchen wastewater containing oil from restaurants and cafeterias has been used to remove oil using floatation due to the difference in specific gravity between oil and water using a grease strap or the like, and the treated water flows out. I have. In recent years, in restaurants and cafeterias, etc., mechanical washing of dishes and the like is frequently used to save labor, and dishes and the like are washed by using a surfactant and imparting a mechanical stirring action. A high degree of emulsification is formed by micelles, which are aggregates of the above surfactant molecules incorporating dirt such as the above. When the surface active agent is washed with a surfactant, the surface of the surface active agent is negatively charged in the waste water, and the emulsification is stabilized by the repulsive force of the same ions. On the other hand, by adding an aqueous solution of a cationic surfactant to the negatively charged dirt micelles, the micelles are electrically neutralized and the micelles are destroyed. Can be removed.
【0003】[0003]
【発明が解決しようとする課題】ところで、従来の厨房
排水を処理する方法では、乳化液滴径が著しく微細化さ
れているので、前記比重差による浮上分離を利用して油
分除去させることは期待出来そうにない。また、厨房排
水は多量の有機物を含むため細菌により、ことに夏季に
腐敗しやすいので悪臭を発生させるものの消臭のための
考慮がなされていない。また、上記カチオン性界面活性
剤は毒性が強く、しかも高価であるので、厨房排水の上
記ミセルの破壊には適用出来ない虞れがある。本発明
は、乳化された油脂分をアルミニウムまたは鉄など2価
または3価の金属および銅の溶解電極による電気分解に
より浮上分離させて分離除去させるとともに腐敗菌の殺
菌と悪臭の発生を防止させることができる厨房排水の油
水分離方法と装置を提供することを目的とする。By the way, in the conventional method of treating kitchen wastewater, the diameter of emulsified droplets is remarkably miniaturized. Therefore, it is expected that the oil content can be removed by utilizing the floating separation based on the difference in specific gravity. Not likely. In addition, kitchen wastewater contains a large amount of organic matter and is easily rotted in the summer due to bacteria, so that it emits a bad smell. However, no consideration has been given to deodorization. Further, since the cationic surfactant is highly toxic and expensive, it may not be applicable to the destruction of the micelles in kitchen wastewater. The present invention is to separate and remove the emulsified fats and oils by floating separation by electrolysis using a dissolving electrode of a divalent or trivalent metal such as aluminum or iron and copper, and to prevent the sterilization of putrefactive bacteria and the generation of offensive odor. It is an object of the present invention to provide a method and an apparatus for separating oil and water from kitchen wastewater which can be used.
【0004】[0004]
【問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、油脂分と、界面活性剤により乳化された
油脂分とを含む厨房排水の油水分離において、2価また
は3価の金属を溶解電極とする第1電解部と銅を溶解電
極とする第2電解部とにより該排水を電気分解すること
を特徴とする。本発明は、油脂分と、界面活性剤により
乳化された油脂分とを含む厨房排水の油水分離装置にお
いて、該排水を流入させる流入室と、流入室に隣接して
2価または3価の金属を溶解電極とする第1電解部と銅
を溶解電極とする第2電解部を配設し流入室からの該排
水を電気分解させる電解処理室と、電解処理室に隣接し
て電解処理室からの処理水を流出させる流出室とからな
ることを特徴とする。本発明は、第1電解部はアルミニ
ウムまたは鉄を溶解電極とすることを特徴とする。本発
明は、第1電解部および第2電解部の夫々の電極は極性
変換させて厨房排水を電気分解することを特徴とする。
本発明は、第1電解部および第2電解部の夫々の電極の
電源部は上記電極を極性変換させる回路を配設したこと
を特徴とする。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention relates to a divalent or trivalent diluent for kitchen wastewater containing oils and fats and oils and fats emulsified by a surfactant. The wastewater is electrolyzed by a first electrolytic unit using a metal as a melting electrode and a second electrolytic unit using copper as a melting electrode. The present invention relates to an oil / water separator for kitchen wastewater containing a fat and oil and a fat and oil emulsified by a surfactant, wherein an inflow chamber into which the wastewater flows, and a divalent or trivalent metal adjacent to the inflow chamber An electrolytic treatment chamber for dissolving the wastewater from the inflow chamber with a first electrolytic part having a melting electrode as the first electrolytic part and a second electrolytic part having copper as the dissolving electrode; and an electrolytic treatment chamber adjacent to the electrolytic treatment chamber. And an outflow chamber through which the treated water flows out. The present invention is characterized in that the first electrolytic unit uses aluminum or iron as a melting electrode. The present invention is characterized in that each electrode of the first electrolysis unit and the second electrolysis unit is subjected to polarity conversion to electrolyze kitchen wastewater.
The present invention is characterized in that a power supply unit for each electrode of the first electrolytic unit and the second electrolytic unit is provided with a circuit for converting the polarity of the electrode.
【0005】[0005]
【発明の実施の形態】以下に図面を参照にして本発明の
好適な一実施形態について詳細に説明する。図1は、本
発明の一実施形態を示す厨房排水の油水分離装置の全体
構成図,図2は、同電解部の要部平面断面図である。図
1において、10は油水分離装置を示し、槽体1は開口
9を有する仕切板7と開口11を有する仕切板8となり
長手方向に区画され、厨房排水の流れ方向に従い、流入
室2と、電解処理室3と、流出室4とを形成している。
5は流入室2の入口、6は流出室4の出口である。流入
室2の内部にはバスケット17を配設し、厨房排水の侠
雑物などを除去している。電解処理室3には2価または
3価の金属であるアルミニウムまたは鉄を溶解電極とす
る第1電解部12と、銅を溶解電極とする第2電解部1
6とを併設しており、流出室4には挿入管18を配設
し、上記出口6と接続している。上記溶解電極は、いず
れも、棒状などに形成されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A preferred embodiment of the present invention will be described below in detail with reference to the drawings. FIG. 1 is an overall configuration diagram of a kitchen drainage oil / water separation device showing one embodiment of the present invention, and FIG. 2 is a plan cross-sectional view of a main part of the electrolytic portion. In FIG. 1, reference numeral 10 denotes an oil-water separator, and the tank body 1 is divided into a partition plate 7 having an opening 9 and a partition plate 8 having an opening 11, and is partitioned in the longitudinal direction. An electrolytic processing chamber 3 and an outflow chamber 4 are formed.
5 is an inlet of the inflow chamber 2 and 6 is an outlet of the outflow chamber 4. A basket 17 is disposed inside the inflow chamber 2 to remove the mess of kitchen drainage. The electrolytic processing chamber 3 includes a first electrolytic unit 12 having a dissolving electrode of aluminum or iron, which is a divalent or trivalent metal, and a second electrolytic unit 1 having a dissolving electrode of copper.
And an outlet tube 4 is provided in the outflow chamber 4 and connected to the outlet 6. Each of the melting electrodes is formed in a rod shape or the like.
【0006】厨房排水は油脂分と、界面活性剤によるミ
セルにより乳化された油脂分となどを含んでおり、入口
5から流入室2に流入されてバスケット17により厨房
排水の食品くず、スラッジなどの侠雑物を分離補集して
から開口9により連通した電解処理室3に流入される。
続いて第1電解部12に流れて直流印加により電解が行
われ、陽極側からの正(プラス)に帯電している2価ま
たは3価の金属イオンの発生により表面が負(マイナ
ス)に帯電している乳化油滴を電気的に中和して破壊す
る。上記ミセルが破壊されることにより上記界面活性剤
を結合していた乳化油脂分は結合する相手を失い、元始
の油脂分に戻り顕在化して比重差により浮上する。陽極
からのアルミニウムまたは鉄イオンはやがて水中の水素
および酸素と結合して水酸化アルミニウムや水酸化鉄の
ごとき水酸化物となり水素および酸素ガスの微細気泡の
利用により食品かすとともに不溶性の汚濁物質(スカ
ム)となって浮上分離される。浮上した上記油脂分、水
酸化物、食品かすなどのスカムは、手動もしくは図示し
ないスカムスキマーなど慣用された方法を用いて物理的
に除去される。また、厨房排水は電解質である塩分を多
く含有していることもあって電気分解反応を促進しうる
ものである。The kitchen wastewater contains fats and oils, fats and oils emulsified by micelles with a surfactant, and the like. After separating and collecting the contaminants, the contaminants flow into the electrolytic processing chamber 3 communicated with the opening 9.
Subsequently, the current flows into the first electrolysis unit 12 to perform electrolysis by applying a direct current, and the surface is charged negatively (minus) by the generation of positively (positively) charged divalent or trivalent metal ions from the anode side. Emulsified oil droplets are neutralized electrically and destroyed. When the micelles are destroyed, the emulsified fats and oils that have bound the surfactant lose their binding partners, return to the original fats and oils, become apparent, and float due to the difference in specific gravity. Aluminum or iron ions from the anode eventually combine with hydrogen and oxygen in the water to form hydroxides, such as aluminum hydroxide and iron hydroxide, by using fine bubbles of hydrogen and oxygen gas and insoluble pollutants (scum). ) And floated. The floating scum such as oils, hydroxides, food debris, etc. is physically removed manually or by a commonly used method such as a scum skimmer (not shown). In addition, kitchen wastewater can promote the electrolysis reaction because it contains a large amount of salt which is an electrolyte.
【0007】さらに、厨房排水は多量の有機物を含むた
め細菌により、ことに夏季に腐敗しやすいので悪臭を発
生する。上記排水は第1電解部12と併設した第2電解
部16にも流れて、同様に電解が行われ、陽極側からの
銅イオンは腐敗菌の一族である嫌気性の硫酸塩還元菌を
殺菌し、腐敗による悪臭の発生を防止することとなる。Furthermore, kitchen wastewater contains a large amount of organic substances, and is easily rotted by bacteria, particularly in summer, thereby generating a bad smell. The wastewater also flows to the second electrolysis unit 16 provided in parallel with the first electrolysis unit 12, and is similarly electrolyzed. Copper ions from the anode side sterilize anaerobic sulfate-reducing bacteria belonging to a family of putrefactive bacteria. Thus, the generation of offensive odor due to putrefaction is prevented.
【0008】電解処理室3において油水分離を行った処
理水は流出室4に流れ挿入管18を通過して出口6から
次工程に移送される。上記挿入管18はその入口端が槽
体1内の水位以下に位置されており、スカムを含まぬ上
記処理水のみが出口6に流れて、油水分離操作を有効と
させることができる。上記槽体1内の水位は槽体1内部
もしくは外部に配設された水位調整器(図示せず)によ
り調整し、油水分離装置10の流量調整を可能とし、電
気分解反応による油水分離操作を最適とさせることがで
きる。The treated water subjected to oil-water separation in the electrolytic treatment chamber 3 flows into the outflow chamber 4, passes through the insertion pipe 18, and is transferred from the outlet 6 to the next step. The insertion end of the insertion pipe 18 is positioned below the water level in the tank 1, and only the treated water containing no scum flows to the outlet 6, so that the oil / water separation operation can be made effective. The water level in the tank body 1 is adjusted by a water level adjuster (not shown) provided inside or outside the tank body 1 so that the flow rate of the oil-water separator 10 can be adjusted, and the oil-water separation operation by the electrolysis reaction can be performed. Can be optimal.
【0009】図2において、第1電解部12の一実施形
態を示し、陽極および陰極を配設してなる電極15は複
数の穴14を開口した塩化ビニールなどからなる筒状の
案内筒13の内部に配設している。また、上記案内筒1
3の上端、下端は開口されており、上記穴14とともに
排水の流れを規制するとともに、電解反応を確実にして
いて、さらに、第1電解部12の絶縁を行い、手動操作
を安全としている。再び、図1において、19は電源部
を示し、交流電源は整流器により交流−直流変換して上
記第1電解部12および第2電解部16とを接続して、
夫々、直流を供給する。また第1電解部12および第2
電解部16の夫々の電極を周期的に極性を自動変換させ
る回路を備えている。上記回路により溶解電極が溶解に
より損耗し頻繁な電極交換の必要性を回避することがで
きる。FIG. 2 shows an embodiment of the first electrolysis section 12, in which an electrode 15 provided with an anode and a cathode is provided with a cylindrical guide tube 13 made of vinyl chloride or the like having a plurality of holes 14 opened. It is arranged inside. In addition, the guide tube 1
The upper end and the lower end of the opening 3 are opened to regulate the flow of the drainage together with the hole 14 to ensure the electrolytic reaction, and to insulate the first electrolytic unit 12 to make the manual operation safe. Again, in FIG. 1, reference numeral 19 denotes a power supply unit, and the AC power supply performs AC-DC conversion by a rectifier and connects the first electrolytic unit 12 and the second electrolytic unit 16 to each other.
Each supplies a direct current. Further, the first electrolytic unit 12 and the second
A circuit is provided for automatically changing the polarity of each electrode of the electrolytic section 16 periodically. The above circuit can avoid the necessity of frequent electrode replacement due to the dissolving electrode being worn by melting.
【0010】[0010]
【実施例】次に、本発明における油水分離装置の諸元
と、それによって得られる油水分離性能について具体的
に説明する。 電 極 出 力 :DC24V 5A(120Wh) アルミニウム電極:15mm径×167mm長さ 9本
(4A) 銅 電 極 :15mm径×167mm長さ 4本
(1A) 処 理 量 :200 l/hNext, the specifications of the oil / water separator according to the present invention and the oil / water separation performance obtained thereby will be specifically described. Electrode output: DC24V 5A (120Wh) Aluminum electrode: 15mm diameter x 167mm length 9 pieces (4A) Copper electrode: 15mm diameter x 167mm length 4 pieces (1A) Processing amount: 200 l / h
【0011】上記記載の装置および方法を用い、厨房排
水の油水分離処理を実施した結果は第1表の通りであ
る。Table 1 shows the results of oil-water separation of kitchen wastewater using the apparatus and method described above.
【0012】[0012]
【表1】 処理前 処理後 pH 5.9 6.7 BOD 378mg/l 128mg/l COD 140mg/l 25mg/l SS 410mg/l 13mg/l ノルマルヘキサン値 350mg/l 1.0mg/l未満 総菌数 3×107 個/ml 3×105 個/ml 硫酸塩還元菌 中度汚染 未検出 銅イオン濃度 0ppm <3ppmTable 1 Before treatment After treatment pH 5.9 6.7 BOD 378 mg / l 128 mg / l COD 140 mg / l 25 mg / l SS 410 mg / l 13 mg / l Normal hexane value 350 mg / l Less than 1.0 mg / l Total bacteria Number 3 × 10 7 cells / ml 3 × 10 5 cells / ml Sulfate-reducing bacteria Medium contamination Not detected Copper ion concentration 0 ppm <3 ppm
【0013】上記電気分解による油水分離処理によって
ノルマルヘキサン値のみならず、SS、BOD、COD
も大幅に低下し、pHも向上することが確認された。ま
た、嫌気性の腐敗菌(土壌菌)の一族の硫化物産生菌で
ある硫酸塩還元菌が死滅することが確認され、銅イオン
濃度も下水道本管に排水するための規制値をクリアして
いることが確認されている。電気消費量も僅少であって
120Wh程度であった。また、スカムの除去は手動に
より1日当たり2〜3回行った。[0013] The oil-water separation treatment by the electrolysis described above not only normal hexane value but also SS, BOD, COD.
Was significantly reduced, and the pH was also confirmed to be improved. In addition, it was confirmed that sulfate-reducing bacteria, a sulfide-producing bacterium of the family of anaerobic putrefactive bacteria (soil fungi), were killed, and the copper ion concentration cleared the regulation value for draining to sewer mains. Has been confirmed. Electricity consumption was also small, about 120 Wh. The removal of scum was manually performed two or three times a day.
【0014】[0014]
【発明の効果】以上説明したように、本発明にかかる厨
房排水の油水分離方法と装置は、乳化された油脂分をア
ルミニウムまたは鉄および銅の溶解電極による電気分解
により浮上分離させるととともに腐敗菌の殺菌と悪臭の
発生を防止させることができる。浮上したスカムの除去
も容易であり、設備費も低廉で、所要スペースも少な
く、低電気消費量にて高い除去効率のもとで運転を行え
るようにしたもので、レストランや食堂等からの厨房排
水に利用し得て、その操作性、環境保全、利便性等を向
上できる等の優れた効果を奏する。As described above, the method and apparatus for separating oil and water from kitchen wastewater according to the present invention floats and separates emulsified fats and oils by electrolysis using aluminum or iron and copper dissolving electrodes, as well as putrefactive bacteria. Sterilization and generation of offensive odor can be prevented. It is easy to remove the scum that has surfaced, the equipment cost is low, the space required is small, the operation can be performed with low electricity consumption and high removal efficiency, and kitchens from restaurants and canteens etc. It can be used for drainage and has excellent effects such as improved operability, environmental protection, and convenience.
【図1】本発明の一実施形態を示す厨房排水の油水分離
装置の全体構成図である。FIG. 1 is an overall configuration diagram of an oil / water separation device for kitchen drainage showing an embodiment of the present invention.
【図2】同電解部の要部平面断面図である。FIG. 2 is a plan cross-sectional view of a main part of the electrolysis unit.
2 流入室 3 電解処理室 4 流出室 10 油水分離装置 12 第1電解部 15 電極 16 第2電解部 19 電源部 Reference Signs List 2 inflow chamber 3 electrolytic treatment chamber 4 outflow chamber 10 oil / water separator 12 first electrolysis section 15 electrode 16 second electrolysis section 19 power supply section
Claims (6)
油脂分とを含む厨房排水の油水分離において、2価また
は3価の金属を溶解電極とする第1電解部と銅を溶解電
極とする第2電解部とにより該排水を電気分解すること
を特徴とする厨房排水の油水分離方法。In a method of separating oil from a kitchen wastewater containing an oil and fat component and an oil and fat component emulsified by a surfactant, a first electrolytic portion having a divalent or trivalent metal as a dissolving electrode and copper as a dissolving electrode. An oil-water separation method for kitchen wastewater, wherein the wastewater is electrolyzed by a second electrolytic part.
油脂分とを含む厨房排水の油水分離装置において、該排
水を流入させる流入室と、流入室に隣接して2価または
3価の金属を溶解電極とする第1電解部と銅を溶解電極
とする第2電解部を配設し流入室からの該排水を電気分
解させる電解処理室と、電解処理室に隣接して電解処理
室からの処理水を流出させる流出室とからなることを特
徴とする厨房排水の油水分離装置。2. An oil / water separator for kitchen wastewater containing oils and fats and oils and fats emulsified by a surfactant, comprising: an inflow chamber into which the wastewater flows, and a divalent or trivalent water adjoining the inflow chamber. An electrolytic processing chamber for dissolving the wastewater from the inflow chamber by disposing a first electrolytic section using metal as a melting electrode and a second electrolytic section using copper as a melting electrode; and an electrolytic processing chamber adjacent to the electrolytic processing chamber An oil / water separation device for kitchen drainage, comprising an outflow chamber for discharging treated water from a kitchen.
解電極とすることを特徴とする請求項第1項に記載の厨
房排水の油水分離方法。3. The method according to claim 1, wherein the first electrolytic unit uses aluminum or iron as a melting electrode.
解電極とすることを特徴とする請求項第2項に記載の厨
房排水の油水分離装置。4. The apparatus according to claim 2, wherein the first electrolysis unit uses aluminum or iron as a melting electrode.
電極は極性変換させて厨房排水を電気分解することを特
徴とする請求項第1項または第3項に記載の厨房排水の
油水分離方法。5. The kitchen drainage according to claim 1, wherein the first electrolysis section and the second electrolysis section each perform a polarity conversion on the respective electrodes to electrolyze the kitchen drainage. Oil-water separation method.
極の電源部は上記電極を極性変換させる回路を配設した
ことを特徴とする請求項第2項または第4項に記載の厨
房排水の油水分離装置。6. The power supply section of each electrode of the first electrolytic section and the second electrolytic section is provided with a circuit for converting the polarity of the electrode. Oil / water separator for kitchen drainage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9027268A JPH10202007A (en) | 1997-01-27 | 1997-01-27 | Oil separation of kitchen waste water and device therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9027268A JPH10202007A (en) | 1997-01-27 | 1997-01-27 | Oil separation of kitchen waste water and device therefor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10202007A true JPH10202007A (en) | 1998-08-04 |
Family
ID=12216340
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9027268A Pending JPH10202007A (en) | 1997-01-27 | 1997-01-27 | Oil separation of kitchen waste water and device therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10202007A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020004661A (en) * | 2000-07-07 | 2002-01-16 | 박영규 | Waste Water Treatment Apparatus using Cylindrical Electrocoagulated Equipment |
CN102642968A (en) * | 2012-04-26 | 2012-08-22 | 卢瑞琳 | Oil-water-solid separation device for kitchen wastes |
JP2019030833A (en) * | 2017-08-07 | 2019-02-28 | 株式会社ヒダン | Oil-water separator and oil-water separation method |
CN114715975A (en) * | 2022-06-09 | 2022-07-08 | 青岛儒海船舶工程有限公司 | Based on two second type boats and ships are repaired with two-way treatment facility of oily water |
-
1997
- 1997-01-27 JP JP9027268A patent/JPH10202007A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020004661A (en) * | 2000-07-07 | 2002-01-16 | 박영규 | Waste Water Treatment Apparatus using Cylindrical Electrocoagulated Equipment |
CN102642968A (en) * | 2012-04-26 | 2012-08-22 | 卢瑞琳 | Oil-water-solid separation device for kitchen wastes |
JP2019030833A (en) * | 2017-08-07 | 2019-02-28 | 株式会社ヒダン | Oil-water separator and oil-water separation method |
CN114715975A (en) * | 2022-06-09 | 2022-07-08 | 青岛儒海船舶工程有限公司 | Based on two second type boats and ships are repaired with two-way treatment facility of oily water |
CN114715975B (en) * | 2022-06-09 | 2022-09-16 | 青岛儒海船舶工程有限公司 | Based on two second type boats and ships are repaired with two-way treatment facility of oily water |
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