JP2006198600A - Method and apparatus for oil-water separation and washing - Google Patents
Method and apparatus for oil-water separation and washing Download PDFInfo
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- JP2006198600A JP2006198600A JP2005041273A JP2005041273A JP2006198600A JP 2006198600 A JP2006198600 A JP 2006198600A JP 2005041273 A JP2005041273 A JP 2005041273A JP 2005041273 A JP2005041273 A JP 2005041273A JP 2006198600 A JP2006198600 A JP 2006198600A
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- 239000001293 FEMA 3089 Substances 0.000 description 1
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 1
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- OMOVVBIIQSXZSZ-UHFFFAOYSA-N [6-(4-acetyloxy-5,9a-dimethyl-2,7-dioxo-4,5a,6,9-tetrahydro-3h-pyrano[3,4-b]oxepin-5-yl)-5-formyloxy-3-(furan-3-yl)-3a-methyl-7-methylidene-1a,2,3,4,5,6-hexahydroindeno[1,7a-b]oxiren-4-yl] 2-hydroxy-3-methylpentanoate Chemical compound CC12C(OC(=O)C(O)C(C)CC)C(OC=O)C(C3(C)C(CC(=O)OC4(C)COC(=O)CC43)OC(C)=O)C(=C)C32OC3CC1C=1C=COC=1 OMOVVBIIQSXZSZ-UHFFFAOYSA-N 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
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- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
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- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 1
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- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
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- 239000001023 inorganic pigment Substances 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 229940057995 liquid paraffin Drugs 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
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- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
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Abstract
Description
本発明は、油水分離方法に関するものであり、各種廃液、廃油、排水の処理方法に関するものである。 The present invention relates to an oil-water separation method, and relates to a method for treating various waste liquids, waste oil, and waste water.
各種廃液、廃油、排水には、油性液体と水性液体と汚染物質としての油性物質や固体懸濁物質が混在するのが一般的である。これらを分離精製して、有用な成分はリュース、リサイクルし、水を一般下水道や河川に排水するには、高価で複雑な廃液処理装置と工程を経る必要がある。特に、溶剤や水を多用し混在する印刷洗浄廃液、塗装廃液、各種洗浄工程廃液、各種精製工程廃液等において問題が大きい。高価で大面積を要する廃液処理装置を導入することが困難な中小企業においては、産業廃棄物として廃棄物処理業者へ処理を依頼することが常であり、高額な処理コストとリュース、リサイクルできない損失は大きなものである。また、その損失は地球環境の規模で考えると莫大なものであり、有効に循環利用できる技術が求められている。 In various waste liquids, waste oils, and wastewaters, oily liquids, aqueous liquids, and oily substances and solid suspended substances as contaminants are generally mixed. In order to separate and purify these components and to recycle and recycle useful components, and to drain water into general sewers and rivers, it is necessary to go through expensive and complex waste liquid treatment equipment and processes. In particular, there is a large problem in printing cleaning waste liquid, coating waste liquid, various cleaning process waste liquid, various purification process waste liquid, etc., which are mixed with a lot of solvents and water. In small and medium-sized enterprises that are difficult to introduce expensive waste liquid treatment equipment that requires a large area, it is usual to request waste disposal companies to treat them as industrial waste. Is a big one. In addition, the loss is enormous considering the scale of the global environment, and a technology that can be effectively recycled is required.
従来、油水分離して汚染物質を除去するには各種の技術がある。たとえば、極細繊維を不織布状にした油水分離フィルターがあるが、対象とする液の性状が限られ、粘稠な汚染物質や目詰まりを起こす固体懸濁物質が混在する場合は適当でない。また、蒸留精製は水と油性物質が共沸する場合が多く、イニシャルコスト・ランニングコストともに高くなる。無機塩や高分子等の凝集剤の使用は、対象とする廃液ごとに最適化が必要であり、スラッジや処理水中の凝集剤や薬剤等処理しなければならない新たな廃棄物を発生する場合が多い。排水処理に凝集剤を利用する例は多いが、油性物質を多量に含む廃油や廃液の油水分離洗浄回収には使われていなかった。
本発明は各種廃液、廃油、排水の処理方法に関するものであり、簡便で汎用性があり、イニシャルコストもランニングコストも低く、設置面積が小さく、有用な成分を循環利用でき、産業廃棄物の排出を最少化し、排水を浄化する方法及び装置を提供せんとするものである。 The present invention relates to a method for treating various waste liquids, waste oils, and wastewaters, is simple and versatile, has a low initial cost and a low running cost, has a small installation area, can circulate useful components, and discharge industrial waste. And to provide a method and apparatus for purifying waste water.
本発明者は、印刷洗浄廃液の処理を検討する過程で、芳香族炭化水素を主成分とする洗浄剤と廃インキ及び湿し水等が混在する系に、親油性表面処理した無機物質微粒子を添加し、撹拌混合し静置すると、清澄な油性液体と廃インキを含む水性液体の2層に分離することを見いだし、本発明を完成するに至った。 In the process of examining the treatment of printing cleaning waste liquid, the present inventor used inorganic substance fine particles subjected to lipophilic surface treatment in a system in which a cleaning agent mainly composed of aromatic hydrocarbons and waste ink and fountain solution are mixed. It was found that when added, stirred and allowed to stand, it was separated into two layers of a clear oily liquid and an aqueous liquid containing waste ink, and the present invention was completed.
すなわち、本発明は油性液体と水性液体と油性物質が混在する状態に、無機物質微粒子を添加して、撹拌混合した後、静置することにより、無機物質微粒子と油性物質が水性液体相に移動して、油性液体と水性液体を2層分離することを特徴とする油水分離洗浄方法であり、その方法を用いた油水分離洗浄装置である。 That is, according to the present invention, inorganic fine particles are added to an oily liquid, an aqueous liquid, and an oily substance, and the mixture is stirred and mixed. An oil-water separation and cleaning method characterized by separating an oily liquid and an aqueous liquid into two layers, and an oil-water separation and cleaning device using the method.
本発明において油性液体とは、水とは層分離する有機物質を主とする液体であり、各種の溶剤、洗浄剤、潤滑剤、動植物油、鉱物油、モノマー類等をいう。たとえば、トルエン、キシレン、エチルベンゼン、ヘキサン、ヘプタン、ブタン、シクロヘキサン、デカリン、テトラリン、テレピン油、灯油、中高沸点石油系溶剤、流動パラフィン、2−エチルブタノール、オクタノール、シクロヘキサノール、ジエチルエーテル、ジイソプロピルエーテル、メチルイソブチルケトン、ジイソプロピルケトン、ジイソブチルケトン、酢酸エチル、酢酸ブチル、等があり、これらの混合物も可能である。本発明において水性液体とは、油性液体とは層分離する水を主とする液体であり、水、水に可溶な有機物質ないし無機物質を含む水溶液をいう。本発明において、油性液体と水性液体と混在する油性物質とは、印刷インキ、塗料、各種洗浄工程で排出される汚染物質、添加剤、可塑剤、潤滑剤、接着剤、低分子量樹脂類、未硬化樹脂類、液状ゴム、等が含まれる。これら油性物質には、無機顔料や充填剤等が包含されていてもかまわない。これら油性物質は、洗浄精製されるべき油性液体よりも粘稠であることが好ましい。また、この液体中には各種の無機物質や有機物質や微生物の固体状微粒子ないし固体懸濁物質が異物や汚れとして混入していてもかまわない。 In the present invention, the oily liquid is a liquid mainly composed of an organic substance that separates layers from water, and refers to various solvents, cleaning agents, lubricants, animal and vegetable oils, mineral oils, monomers, and the like. For example, toluene, xylene, ethylbenzene, hexane, heptane, butane, cyclohexane, decalin, tetralin, turpentine oil, kerosene, medium and high boiling petroleum solvent, liquid paraffin, 2-ethylbutanol, octanol, cyclohexanol, diethyl ether, diisopropyl ether, There are methyl isobutyl ketone, diisopropyl ketone, diisobutyl ketone, ethyl acetate, butyl acetate, and the like, and mixtures thereof are also possible. In the present invention, the aqueous liquid is a liquid mainly composed of water that is separated into layers, and refers to an aqueous solution containing water, an organic substance or an inorganic substance soluble in water. In the present invention, oily substances mixed with oily liquids and aqueous liquids include printing inks, paints, contaminants discharged in various cleaning processes, additives, plasticizers, lubricants, adhesives, low molecular weight resins, Cured resins, liquid rubber, etc. are included. These oily substances may include inorganic pigments and fillers. These oily substances are preferably more viscous than the oily liquid to be washed and refined. In addition, various inorganic substances, organic substances, solid fine particles or solid suspended substances of microorganisms may be mixed in the liquid as foreign matters or dirt.
本発明において、無機物質微粒子とは、天然もしくは合成の水に不溶の無機粉末をいう。たとえば、膠質炭酸カルシウム(沈降性炭酸カルシウムともいう)、軽微性炭酸カルシウム、重質炭酸カルシウム、多孔質炭酸カルシウム、硫酸カルシウム、水酸化アルミニウム、水酸化マグネシウム、シリカ、珪酸マグネシウム、珪酸アルミニウム、カオリン、タルクその他粘土鉱物類が可能であり、合成ゴムや合成樹脂に充填剤として使用される無機粉末が安全性、汎用性、価格等の点で好適であり、廃棄物の二次公害がない点でも望ましい。本発明の無機物質微粒子の平均粒子径は通常10ミクロン以下が好ましく、特に3ミクロン以下が望ましい。たとえば、平均粒子径1ミクロン程度の軽微性炭酸カルシウム、平均粒子径2ミクロンで表面がステアリン酸カルシウムで被覆された重質炭酸カルシウムは好適である。また特に、平均粒子径が0.1ミクロン以下の無機物質微粒子も好ましい。たとえば、平均粒子径0.08ミクロン程度の膠質炭酸カルシウムは好適である。平均粒子径の下限は特に規定されるべきものではなく、粉体の取扱い易さも加味して選択できる。平均粒子径以外にも、比表面積や吸油量の大きいものを基準に選択することも可能である。吸油量の大きい、平均粒子径1〜10ミクロンの範囲にある多孔質炭酸カルシウムは特に好適である。
また、無機物質微粒子の表面は親油性処理がなされていることが好ましい。親油性表面処理には、ステアリン酸やステアリン酸カルシウムのように親油性基と極性基を含む化合物で、無機物質微粒子表面を被覆処理することにより得られる。また、高分子量の界面活性剤や極性基をもつ有機高分子で無機物質微粒子表面を被覆処理することにより得られる。また、膠質炭酸カルシウムや軽微性炭酸カルシウムのように、親油性基と極性基を含む化合物の存在下で消石灰水溶液に炭酸ガスを吹き込み、炭酸カルシウム結晶を生成させることによっても得られる。
無機物質微粒子の選定は、浄化の対象となる各種廃液、廃油、排水の性状によって適宜最適なものを選定できるが、無機物質微粒子が液体中に浮遊拡散する油性物質を凝集し、固体懸濁物質も取り込みながら、自重を増して沈降するメカニズムを想定すれば、選定は容易である。ただし、無機物質微粒子の親油性が大きすぎる場合は、無機物質微粒子が液体中に浮遊拡散する油性物質を凝集し、固体懸濁物質も取り込みながら、沈降せずに油性液体層に集中することが起こる。この場合は、水性液体の浄化に好適である。In the present invention, inorganic fine particles refer to inorganic powders that are insoluble in natural or synthetic water. For example, colloidal calcium carbonate (also called precipitated calcium carbonate), light calcium carbonate, heavy calcium carbonate, porous calcium carbonate, calcium sulfate, aluminum hydroxide, magnesium hydroxide, silica, magnesium silicate, aluminum silicate, kaolin, Talc and other clay minerals are possible, and inorganic powders used as fillers in synthetic rubber and synthetic resin are suitable in terms of safety, versatility, price, etc., and there is no secondary pollution of waste desirable. The average particle size of the inorganic fine particles of the present invention is usually preferably 10 microns or less, and particularly preferably 3 microns or less. For example, light calcium carbonate having an average particle diameter of about 1 micron and heavy calcium carbonate having an average particle diameter of 2 microns and coated with calcium stearate are preferable. In particular, inorganic fine particles having an average particle size of 0.1 microns or less are also preferable. For example, colloidal calcium carbonate having an average particle size of about 0.08 microns is suitable. The lower limit of the average particle diameter is not particularly specified, and can be selected in consideration of ease of handling of the powder. In addition to the average particle diameter, it is possible to select based on a specific surface area or a large oil absorption amount. Porous calcium carbonate having a large oil absorption and an average particle diameter in the range of 1 to 10 microns is particularly suitable.
Moreover, it is preferable that the surface of the inorganic fine particles is subjected to lipophilic treatment. The lipophilic surface treatment can be obtained by coating the surface of the inorganic substance fine particles with a compound containing a lipophilic group and a polar group such as stearic acid or calcium stearate. Further, it can be obtained by coating the surface of inorganic fine particles with a high molecular weight surfactant or an organic polymer having a polar group. It can also be obtained by blowing carbon dioxide into an aqueous solution of slaked lime in the presence of a compound containing a lipophilic group and a polar group, such as colloidal calcium carbonate and light calcium carbonate, to produce calcium carbonate crystals.
The selection of inorganic fine particles can be selected as appropriate depending on the properties of various waste liquids, waste oil, and wastewater to be purified, but the inorganic fine particles agglomerate oily substances that float and diffuse in the liquid, resulting in solid suspended substances. Selection is easy if we assume a mechanism that sinks by increasing its own weight while taking in water. However, if the inorganic substance fine particles are too lipophilic, the inorganic substance fine particles may aggregate oily substances that float and diffuse in the liquid and concentrate in the oily liquid layer without sinking while taking in solid suspended solids. Occur. In this case, it is suitable for purification of an aqueous liquid.
本発明において、油水分離洗浄する方法とは、油性液体と水性液体と油性物質が混在する状態に、無機物質微粒子を添加して、撹拌混合した後、静置することにより、無機物質微粒子と油性物質が凝集して水性液体相に移動して、油性液体と水性液体を2層分離することにより達成される。無機物質微粒子を添加する量は、油性液体と水性液体と油性物質の量及び撹拌混合の強度によって適宜決められるが、油性物質の1/10から100倍の重量比の範囲の量が好ましく、1/2から10倍の重量比の範囲が更に好ましい。また、油性液体と水性液体と油性物質が混在する液体総量100重量部に対しては、無機物質微粒子0.1〜10重量部が好ましく、1〜5重量部が更に好ましい。
撹拌混合するには通常の撹拌混合槽が利用でき、容器全体を振とうすることも可能である。必要なことは、油性液体と水性液体と油性物質及び無機物質微粒子が均一に混合されることであり、混合されない死角を容器内につくらないことである。また、無機物質微粒子が油性物質の全てを凝集できるほど激しい撹拌、強い振とうが望ましい。撹拌混合後の静置する時間は、油性液体と水性液体が2層に分離するまで必要であり、油性液体層に浮遊する無機物質微粒子と油性物質が水性液体相に移動して、油性液体層が清澄になるまで待つことが望ましい。2層分離した清澄な油性液体と、無機物質微粒子と油性物質が凝集混入した水性液体は、各種方法で分液される。当然のことながら、清澄になった油性液体を循環利用する場合は、無機物質微粒子と油性物質が集中混入した水性液体の混入を避けて分取すべきである。この方法により、蒸留精製することなく、簡便に循環利用可能な油性液体を回収することができる。
回収した油性液体は、再使用前にろ過するのは好ましい。一方、無機物質微粒子と油性物質が集中混入した水性液体は、遠心分離やろ過等の方法で、水性液体と油性物質を包含する無機物質のケーク状塊に分離できる。水性液体は循環利用するか、排水基準を満たすまで浄化されていれば下水道や河川へ排水できる。また遠心分離やろ過をせずに、自然乾燥で油性物質を包含する無機物質のケーク状塊にして、減容できる。油性物質を包含する無機物質のケーク状塊は循環利用できなければ、産業廃棄物として規定の処理がなされることになるが、当初の油性液体と水性液体と油性物質が混在する状態に比して、著しく減容されており、廃棄物処理コストは著しく軽減され、地球環境負荷も小さくなったと言える。In the present invention, the oil-water separation and cleaning method is a method of adding inorganic fine particles to a state where an oily liquid, an aqueous liquid, and an oily substance are mixed, stirring and mixing, and then allowing to stand, whereby the inorganic fine particles and the oily This is accomplished by agglomerating and moving the substance into the aqueous liquid phase and separating the oily liquid and the aqueous liquid into two layers. The amount of inorganic fine particles added is appropriately determined according to the amount of oily liquid, aqueous liquid and oily material, and the strength of stirring and mixing, but is preferably in the range of 1/10 to 100 times the weight ratio of the oily material. A weight ratio in the range of / 2 to 10 times is more preferable. Moreover, 0.1-10 weight part of inorganic substance microparticles | fine-particles are preferable with respect to 100 weight part of liquid total in which an oily liquid, an aqueous liquid, and an oily substance are mixed, and 1-5 weight part is still more preferable.
For stirring and mixing, a normal stirring and mixing tank can be used, and the entire container can be shaken. What is necessary is that the oily liquid, the aqueous liquid, the oily substance, and the inorganic substance fine particles are uniformly mixed, and no dead angle that is not mixed is created in the container. Moreover, vigorous stirring and strong shaking are desirable so that the inorganic substance fine particles can aggregate all of the oily substance. The time to stand after stirring and mixing is necessary until the oily liquid and the aqueous liquid are separated into two layers, and the inorganic substance fine particles and the oily substance floating in the oily liquid layer move to the aqueous liquid phase, and the oily liquid layer It is desirable to wait until is clear. The clear oily liquid separated into two layers and the aqueous liquid in which the inorganic substance fine particles and the oily substance are coagulated and mixed are separated by various methods. As a matter of course, when the clarified oily liquid is circulated and used, it should be separated while avoiding the mixing of the aqueous liquid in which inorganic fine particles and the oily substance are intensively mixed. By this method, an oily liquid that can be easily circulated can be recovered without being purified by distillation.
The recovered oily liquid is preferably filtered before reuse. On the other hand, an aqueous liquid in which inorganic fine particles and an oily substance are concentrated and mixed can be separated into a cake-like lump of an inorganic substance including an aqueous liquid and an oily substance by a method such as centrifugation or filtration. Aqueous liquids can be circulated or drained into sewers and rivers if they are purified until they meet drainage standards. In addition, the volume can be reduced to a cake-like lump of inorganic substance including oily substance by natural drying without centrifugation or filtration. If the cake-like lump of inorganic substance including oily substance cannot be recycled, it will be treated as industrial waste, but compared to the original oily liquid, aqueous liquid and oily substance mixed. Therefore, it can be said that the volume of waste treatment has been remarkably reduced, and the burden on the global environment has been reduced.
本発明の実施の態様は上記に限定されるものではない。油性液体のみに汚染物質として粘稠な油性物質が混入している場合、清澄な油性液体を回収するために、適量の水と無機物質微粒子を添加し、撹拌混合して、静置することにより、2層分離して清澄な油性液体と、無機物質微粒子と油性物質が凝集混入した水性液体に分離することができる。また、水性液体に混在する油性物質や水に溶けている有機物質を除去するために、適量の油性液体と無機物質微粒子を添加し、撹拌混合して、静置することにより、2層分離して油性液体と、無機物質微粒子と油性物質が凝集混入した水性液体に分離することができ、その水性液体側をろ過ないし遠心分離することによって、水から油性物質を容易に除去することができる。また、本発明の方法は、各種廃液、廃油、排水の処理に限定されるものではなく、各種化学プロセス、食品加工プロセス、医薬製造プロセス等においても油水分離洗浄精製に有用である。 The embodiment of the present invention is not limited to the above. If a viscous oily substance is mixed as a contaminant only in the oily liquid, add an appropriate amount of water and inorganic fine particles, stir and mix, and leave to stand to recover a clear oily liquid. It can be separated into two layers and separated into a clear oily liquid and an aqueous liquid in which inorganic fine particles and an oily substance are coagulated and mixed. In addition, in order to remove oily substances mixed in aqueous liquids and organic substances dissolved in water, an appropriate amount of oily liquids and inorganic fine particles are added, mixed with stirring, and left to stand to separate two layers. Thus, it can be separated into an oily liquid, an aqueous liquid in which inorganic fine particles and an oily substance are aggregated and mixed, and the oily substance can be easily removed from water by filtering or centrifuging the aqueous liquid side. In addition, the method of the present invention is not limited to the treatment of various waste liquids, waste oils, and wastewaters, but is useful for oil-water separation cleaning purification in various chemical processes, food processing processes, pharmaceutical manufacturing processes, and the like.
本発明の方法を使用して油水分離洗浄装置を製作できる。その一つは、図1に示すように、油性液体と水性液体と油性物質が混在する状態に、親油性表面を有する無機物質微粒子を添加して、撹拌混合する機能と、静置する機能、油性液体と水性液体の2層を分離する機能を具備することを特徴とする油水分離洗浄装置である。他の一つは、図2に示すように、油性液体と水性液体と油性物質が混在する状態に、親油性表面を有する無機物質微粒子を添加して、撹拌混合する機能と、静置する機能、油性液体と水性液体の2層を分離する機能、水性液体層から無機物質微粒子と油性物質を分離して水ないし水性液体を得る機能を具備することを特徴とする油水分離洗浄装置である。撹拌混合には撹拌槽内に撹拌されない死角をつくらないことが重要であり、撹拌の代わりに容器全体を振とうすることも可能である。静置時間を短縮したり、無機物質微粒子と油性物質等からなる産業廃棄物の容積を最小化するためにも、分離する機能としては遠心分離が好ましく利用できる。清澄になった油性液体を再利用する場合は、水性液体や無機物質微粒子や油性物質等を再混入させないためには、容器内上層にある油性液体は吸引して取り出すのが望ましく、再使用の前にろ過するのも望ましい。 An oil-water separation and cleaning apparatus can be manufactured using the method of the present invention. For example, as shown in FIG. 1, a function of adding inorganic substance fine particles having a lipophilic surface to a state where an oily liquid, an aqueous liquid and an oily substance are mixed, and a function of stirring and mixing; An oil-water separation and cleaning apparatus having a function of separating two layers of an oily liquid and an aqueous liquid. The other is, as shown in FIG. 2, a function of adding inorganic substance fine particles having a lipophilic surface to a state where an oily liquid, an aqueous liquid and an oily substance are mixed, and a function of stirring and mixing, and a function of standing still An oil / water separation and cleaning apparatus comprising a function of separating two layers of an oily liquid and an aqueous liquid, and a function of separating inorganic fine particles and an oily substance from the aqueous liquid layer to obtain water or an aqueous liquid. For stirring and mixing, it is important not to create a blind spot that is not stirred in the stirring tank, and it is possible to shake the entire container instead of stirring. Centrifugation can be preferably used as a separation function in order to shorten the standing time or to minimize the volume of industrial waste composed of inorganic fine particles and oily substances. When reusing a clarified oily liquid, it is desirable to suck out the oily liquid in the upper layer of the container in order to prevent remixing of aqueous liquids, inorganic fine particles, oily substances, etc. It is also desirable to filter before.
本発明によれば、粘稠な油性物質で汚染された各種の廃液、廃油、排水を、極めて簡単に安価に油水分離して清浄化でき、清浄化された油性液体は再利用が可能となり、水性液体は清浄化して排水が可能になり、産業廃棄物の排出が著しく少なくなる。 According to the present invention, various waste liquids, waste oils, and wastewaters contaminated with viscous oily substances can be separated by oil and water very easily and inexpensively, and the purified oily liquid can be reused. Aqueous liquids can be cleaned and drained, and industrial waste emissions are significantly reduced.
粘稠な油性物質で汚染された各種の廃液、廃油、排水に、親油性表面を有する無機物質微粒子を添加し、撹拌混合し、静置後層分離して上層にある、清澄もしくは清澄に近い状態になった油性液体を分液回収して、必要であればろ過して、再利用するこを、簡単な操作で実現した。
以下に実施例により本発明を説明する。Add fine inorganic substance particles with lipophilic surface to various waste liquids, waste oils, and wastewaters contaminated with viscous oily substances, stir and mix, and after standing, separate the layers, and are in the upper layer, close to clarification or near clarification Separating and collecting the oily liquid in a state, filtering it if necessary, and reusing it was realized with a simple operation.
The following examples illustrate the invention.
オフセット印刷におけるブランケット・ロール洗浄廃液100mlを300ml三角フラスコに入れ、平均粒子径0.08ミクロン、DOP吸油量26.0ml/100gの膠質炭酸カルシウム6g添加して、フラスコを2分間強振して、静置した。洗浄廃液は中高沸点石油系溶剤の洗い油が約80%、水分が約18%、黒色インキ類が約2%混入しており、油層と水の層は2層に分離して見えるが、粘稠な黒色インキ類の油性物質は両層にまたがり汚染している。静置後1時間以内に、上層に清澄で透明な液が現れ、下層の黒色層から分離してくるが、1夜放置すると、上層に清澄で透明な液層約80%と下層に黒色液層約20%に明確に分離した。上層をガスクロにて分析したところ、洗浄液として使用した中高沸点石油系溶剤の洗い油の成分と一致した。下層の黒色液を分離して遠心分離したところ、約7gの黒色固形物と水性液体に分離した。水性液体のCODを簡易試験紙で測定したところ、250ppmであった。 Add 100 ml of blanket / roll cleaning waste liquid in offset printing to a 300 ml Erlenmeyer flask, add 6 g of colloidal calcium carbonate with an average particle size of 0.08 microns and DOP oil absorption of 26.0 ml / 100 g, shake the flask for 2 minutes, I put it. The washing waste liquid contains about 80% washing oil of medium and high boiling point petroleum solvent, about 18% moisture, and about 2% black ink. The oil layer and water layer appear to separate into two layers. The oily substance of thick black ink is contaminated across both layers. Within 1 hour after standing, a clear and transparent liquid appears in the upper layer and separates from the lower black layer. If left overnight, the clear and transparent liquid layer is about 80% in the upper layer and the black liquid in the lower layer. Clearly separated into about 20% layer. When the upper layer was analyzed by gas chromatography, it coincided with the components of the washing oil of the medium and high boiling point petroleum solvent used as the washing liquid. When the lower layer black liquid was separated and centrifuged, it was separated into about 7 g of a black solid and an aqueous liquid. It was 250 ppm when COD of aqueous liquid was measured with the simple test paper.
実施例1で使用した洗浄廃液と下記の各種無機物質微粒子を、実施例1と同様にして添加し、撹拌混合し、静置して2層分離の状況を観察した。いずれの結果も、上層に清澄で透明な中高沸点石油系溶剤の洗い油と、下層に黒色ないし灰色の粘稠な液体の層に分離した。
無機物質微粒子A:軽微性炭酸カルシウム;平均粒子径1.5ミクロン、
無機物質微粒子B:重質炭酸カルシウム;平均粒子径1.5ミクロン、ステアリン酸カルシウム1%表面処理
無機物質微粒子C:多孔質炭酸カルシウム;平均粒子径3ミクロン、
無機物質微粒子D:カオリンクレー;平均粒子径1.5ミクロン、
無機物質微粒子E:硫酸カルシウム;平均粒子径1ミクロン、ステアリン酸カルシウム1%表面処理The washing waste liquid used in Example 1 and the following various inorganic substance fine particles were added in the same manner as in Example 1, stirred and mixed, and allowed to stand to observe the state of two-layer separation. In either case, the upper layer was separated into a clear and transparent medium-high boiling petroleum solvent washing oil in the upper layer and a black to gray viscous liquid layer in the lower layer.
Inorganic substance fine particles A: light calcium carbonate; average particle size 1.5 microns,
Inorganic substance fine particles B: heavy calcium carbonate; average particle size 1.5 microns, calcium stearate 1% surface-treated inorganic material fine particles C: porous calcium carbonate; average particle size 3 microns,
Inorganic substance fine particle D: Kaolin clay; average particle size 1.5 microns,
Inorganic substance fine particle E: calcium sulfate; average particle diameter 1 micron, calcium stearate 1% surface treatment
溶剤や水を多用し混在する印刷洗浄廃液、塗装廃液、各種洗浄工程廃液、各種精製工程廃液等において、有用な成分はリュース、リサイクルし、水は一般下水道や河川に排水できる、安価で、簡便で、省スペースの廃液処理方法として有用である。 Useful components such as printing washing waste liquid, painting waste liquid, various washing process waste liquid, various purification process waste liquid, etc., which are mixed with a lot of solvents and water, are useful and recycled, and the water can be drained into general sewers and rivers at low cost and simple. Thus, it is useful as a space-saving waste liquid treatment method.
A 油性液体と水性液体と油性物質が混在する液体
B 無機物質微粒子
C 再利用可能な油性液体
D 水性液体+油性物質+無機物質微粒子
E 水性液体
F 油性物質+無機物質微粒子A A mixture of oily liquid, aqueous liquid, and oily substance B Inorganic substance fine particle C Reusable oily liquid D Aqueous liquid + oily substance + inorganic substance fine particle E Aqueous liquid F Oily substance + inorganic substance fine particle
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| JP2005041273A JP2006198600A (en) | 2005-01-20 | 2005-01-20 | Method and apparatus for oil-water separation and washing |
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| JP2006198600A true JP2006198600A (en) | 2006-08-03 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2015000385A (en) * | 2013-06-17 | 2015-01-05 | 株式会社東芝 | Water treatment method using filter aid, and device for the method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2015000385A (en) * | 2013-06-17 | 2015-01-05 | 株式会社東芝 | Water treatment method using filter aid, and device for the method |
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