JP2003010681A - Oil removing agent and oil removing method and apparatus - Google Patents

Oil removing agent and oil removing method and apparatus

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Publication number
JP2003010681A
JP2003010681A JP2001200864A JP2001200864A JP2003010681A JP 2003010681 A JP2003010681 A JP 2003010681A JP 2001200864 A JP2001200864 A JP 2001200864A JP 2001200864 A JP2001200864 A JP 2001200864A JP 2003010681 A JP2003010681 A JP 2003010681A
Authority
JP
Japan
Prior art keywords
oil
containing liquid
liquid waste
parts
carbide
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
JP2001200864A
Other languages
Japanese (ja)
Inventor
Norihiro Yaide
乃大 矢出
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP2001200864A priority Critical patent/JP2003010681A/en
Publication of JP2003010681A publication Critical patent/JP2003010681A/en
Pending legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain an oil removing agent capable of removing oil from oil- containing liquid waste stably and effectively, and an oil removing method and an apparatus using the same. SOLUTION: The oil removing agent comprises 100 pts.wt. of chemical synthetic fibers and 5-50 pts.wt. of carbide particles with a particle size of several-100 μm or comprises 100 pts.wt. of chemical synthetic fibers, 1-20 pts.wt. of a surfactant or an organic polymeric flocculant and 5-50 pts.wt. of carbide particles with a particle size of several-100 μm. In the oil removing method, the oil removing agent and oil-containing liquid waste being matter to be treated are mixed to separate oil from the matter to be treated, or carbide and oil- containing liquid waste being matter to be treated are mixed and chemical synthetic fibers are added to the resulting mixture to separate oil from the matter to be treated.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、含油液状廃棄物か
らの油除去に係り、特に、下水、し尿、産業排水又はそ
れらの排水処理に伴って発生する汚泥や、生ごみ等の廃
棄物に含まれる油を分離する油除去剤と、それを用いて
含油液状廃棄物から油を除去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 oil removal from oil-containing liquid wastes, and particularly to wastes such as sewage, night soil, industrial wastewater or sludge generated by the wastewater treatment, and garbage. TECHNICAL FIELD The present invention relates to an oil removing agent for separating contained oil, and a method and an apparatus for removing oil from an oil-containing liquid waste using the same.

【0002】[0002]

【従来の技術】下水、し尿、産業排水等に含まれる油
は、凝集沈殿処理での汚泥の浮上や、スクリーン分離で
のスクリーンの目詰まりや、生物処理における発泡やス
カムの原因となるために、予め除去しておくのが一般的
である。下水、し尿、産業排水等の排水処理に伴って発
生する汚泥や、生ごみ等や産業廃棄物に含まれる油の処
理は、重要である。これらの含油液状廃棄物は、そのま
ま放置すると、含まれる油の分解による臭気発生、脱水
処理における含水率に見られる脱水性能の低下、あるい
は嫌気性発酵処理においてスカムや発酵処理阻害の問題
が生じる。特に、下水、し尿、産業排水等や排水処理に
伴って発生する有機性汚泥や、生ごみ等の有機性廃棄物
を含む含油液状廃棄物は、臭気の発生が顕著で、処理設
備の作業環境の悪化や中間処理における処理性能の低下
が見られる。
BACKGROUND OF THE INVENTION Oil contained in sewage, night soil, industrial wastewater, etc. causes flotation of sludge during coagulation sedimentation, clogging of screen during screen separation, and foaming and scum in biological treatment. , It is generally removed in advance. It is important to treat sludge generated by wastewater treatment such as sewage, night soil, and industrial wastewater, and oil contained in food waste and industrial waste. When these oil-containing liquid wastes are left as they are, problems such as generation of odor due to decomposition of contained oil, deterioration of dehydration performance seen in water content in dehydration treatment, or scum and inhibition of fermentation treatment in anaerobic fermentation treatment occur. In particular, sewage, night soil, industrial wastewater, etc. and organic sludge generated by wastewater treatment, and oil-containing liquid waste including organic waste such as kitchen waste generate significant odor, and the working environment of the treatment facility And deterioration of processing performance in intermediate processing.

【0003】含油液状廃棄物の油の除去方法としては、
静置させて、液面に浮上する油を人力で除去するか、ス
クリーンによる分離が挙げられる。それが流動性の高い
鉱物油、潤滑油などであれば、市販のオイルマットによ
る吸着処理が可能である。動植物油に対しては、ビルピ
ットに流入する油に対して、油分解酵素であるリパーゼ
を含む生物製剤が実用化されている。常温で固形状にな
る動植物油は、スクリーン分離に際して、スクリーンを
閉塞させて、油除去の作業性を著しく低下させる。ま
た、分離した油のハンドリングが非常に悪い。このよう
な、従来より提案されている方法は、以下のような問題
点がある。 (1) 単に含油液状廃棄物をスクリーンで分離する方
法は、常温で固形状の油が対象で、乳化油や細かく分散
した油には適用できない。 (2) スクリーン分離法では、対象油によるスクリー
ンの閉塞や分離油のハンドリング、その処分に問題が多
い。 (3) リパーゼを含む生物製剤は、その油分解反応が
緩慢であるために、大量の含油液状廃棄物を短期間に処
理することが困難である。
As a method for removing oil from oil-containing liquid waste,
For example, the oil that floats on the surface of the liquid can be removed manually by allowing it to stand still, or separation with a screen can be used. If it is a highly fluid mineral oil or lubricating oil, it can be adsorbed by a commercially available oil mat. For animal and vegetable oils, biopharmaceuticals containing lipase, which is an oil-degrading enzyme, have been put into practical use for oils flowing into bill pits. Animal and vegetable oils that become solid at room temperature clog the screen during screen separation and significantly reduce the workability of oil removal. Also, the handling of the separated oil is very poor. Such a method conventionally proposed has the following problems. (1) The method of simply separating the oil-containing liquid waste by a screen is intended for solid oils at room temperature, and cannot be applied to emulsified oils or finely dispersed oils. (2) In the screen separation method, there are many problems in clogging of the screen with the target oil, handling of the separated oil, and disposal thereof. (3) It is difficult to treat a large amount of oil-containing liquid waste in a short period of time because the biodegradation product containing lipase has a slow oil decomposition reaction.

【0004】[0004]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解消し、含油液状廃棄物から安定して効果
的に油を除去できる油除去剤と、それを用いる油除去方
法と装置を提供することを課題とする。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art and is capable of stably and effectively removing oil from oil-containing liquid waste, and an oil removing method using the same. An object is to provide a device.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、化学合成繊維100重量部と、数〜1
00μmの炭化物粒子5〜50重量部とからなる油除去
剤、又は、化学合成繊維100重量部と、界面活性剤又
は有機高分子凝集剤1〜20重量部と、数〜100μm
の炭化物粒子5〜50重量部とからなる油除去剤とした
ものである。また、本発明では、前記の油除去剤と、被
処理物である含油液状廃棄物を混合することにより、被
処理物から油を分離することを特徴とする含油液状廃棄
物からの油除去方法とするか、又は、炭化物と、被処理
物である含油液状廃棄物とを混合した後に、化学合成繊
維を添加することにより、被処理物から油を分離するこ
とを特徴とする含油液状廃棄物からの油除去方法とした
ものである。さらに、本発明では、前記の油除去剤と、
被処理物である含油液状廃棄物とを混合する混合装置
と、該混合装置から油を分離する分離装置とを有するこ
とを特徴とする含油液状廃棄物からの油除去装置とした
ものである。前記油を分離する分離装置は、スクリーン
や脱水機を用いることができる。
In order to solve the above-mentioned problems, in the present invention, 100 parts by weight of chemically synthesized fiber and several to 1 parts are used.
Oil remover consisting of 5 to 50 parts by weight of carbide particles of 00 μm, or 100 parts by weight of chemically synthesized fiber, 1 to 20 parts by weight of surfactant or organic polymer coagulant, and several to 100 μm
The oil removing agent comprises 5 to 50 parts by weight of carbide particles. Further, in the present invention, a method for removing oil from an oil-containing liquid waste, characterized in that the oil is separated from the object to be processed by mixing the oil remover with the oil-containing liquid waste to be processed. Or, after mixing the carbonized material and the oil-containing liquid waste that is the object to be processed, the chemically separated fiber is added to separate the oil from the object to be processed. This is the method for removing oil from the. Further, in the present invention, the above oil remover,
An oil removing device for an oil-containing liquid waste, comprising: a mixing device for mixing an oil-containing liquid waste, which is an object to be treated, and a separating device for separating oil from the mixing device. A screen or a dehydrator can be used as the separation device for separating the oil.

【0006】[0006]

【発明の実施の形態】次に、本発明を詳細に説明する。
まず、油除去剤について説明すると、本発明の油除去剤
に使用できる化学合成繊維は、化学繊維製造工程から廃
棄されるポリエステル繊維やポリプロピレン繊維、アク
リロニトリル繊維あるいはPETボトルから得られるポ
リエステル再生繊維等である。化学合成繊維の形状は、
太さが数μm〜1mm、長さが数mm〜数cmである。
細い方が油除去性能や各種薬剤を含浸させるには都合が
よいが、繊維に加工するのが困難である。市販されてい
る化学合成繊維を本発明に使う場合には、その太さは数
〜数十μmが好適である。また、その長さもスラリー状
にしたときの作業性やスクリーンでの分離性能を考慮す
ると、数mm〜1cmが好適である。
BEST MODE FOR CARRYING OUT THE INVENTION Next, the present invention will be described in detail.
First, the oil remover will be described. The chemically synthetic fibers that can be used in the oil remover of the present invention include polyester fibers, polypropylene fibers, acrylonitrile fibers or polyester recycled fibers obtained from PET bottles discarded from the chemical fiber manufacturing process. is there. The shape of chemically synthesized fiber is
The thickness is several μm to 1 mm and the length is several mm to several cm.
A thinner one is more convenient for oil removal performance and impregnation with various chemicals, but it is difficult to process it into fibers. When a commercially available chemically synthesized fiber is used in the present invention, its thickness is preferably several to several tens of μm. Further, the length is preferably several mm to 1 cm in consideration of workability when it is made into a slurry state and separation performance on a screen.

【0007】本発明の油除去剤で化学合成繊維と共に用
いて、該表面に担持させる炭化物は、石炭系、木質系、
ヤシ殻系活性炭やそれらの未再生炭や産業廃棄物や建築
廃材や下水汚泥などから製造された固定炭素が主成分の
炭化物である。本発明に使用される炭化物の物性は、粒
子径だけであり、一般の活性炭などに要求される吸着性
能は必要ない。炭化物の形状は、粉末状で、その粒子径
は、数〜100μmである。炭化物の粒径が小さい方が
油の吸着が良い。化学合成繊維の太さが数〜数十μmで
あるので、担持させる炭化物粒子径は、数〜数十μmが
好適であるが、化学合成繊維間で炭化物粒子が保持でき
ることから最大粒子径は100μmである。
The carbides used on the surface of the oil removing agent of the present invention when used together with chemically synthesized fibers are coal-based, wood-based,
Fixed carbon produced from coconut shell-based activated carbon, unregenerated carbon thereof, industrial waste, construction waste, sewage sludge, etc. is a main component of carbide. The physical property of the carbide used in the present invention is only the particle size, and the adsorption performance required for general activated carbon is not required. The shape of the carbide is powdery, and the particle size thereof is several to 100 μm. The smaller the particle size of carbide, the better the adsorption of oil. Since the thickness of the chemically synthesized fiber is several to several tens μm, the carbide particle diameter to be supported is preferably several to several tens μm, but the maximum particle diameter is 100 μm because the carbide particles can be held between the chemically synthesized fibers. Is.

【0008】本発明で担持とは、化学合成繊維表面に炭
化物粒子が付着している状態である。繊維と炭化物粒子
を担持させることにより、液に油除去剤を添加しても、
液中でも繊維表面に炭化物粒子が付着した状態が維持さ
れる。繊維に炭化物粒子をより強く担持させるために、
界面活性剤や有機高分子凝集剤が使用される。油除去機
構としては、繊維に担持された炭化物粒子に油が付着す
る場合と、フリーの炭化物粒子に油が付着し、この炭化
物が繊維に捕捉される場合がある。化学合成繊維への炭
化物の担持量は、化学合成繊維100重量部あたり乾燥
炭化物は5〜50重量部である。化学合成繊維100重
量部あたり乾燥炭化物は5重量部未満では、油の吸着性
能が不足する。一方、50重量部を超えると化学合成繊
維表面に炭化物を保持することが難しく、炭化物が無駄
になる。更に、化学合成繊維から離れた炭化物は、含油
液状廃棄物の油を吸着するが、油を吸着した炭化物を化
学合成繊維でからめ取ることできず、含油液状廃棄物か
らの油の分離除去が困難である。
The term "supported" in the present invention means a state in which carbide particles adhere to the surface of the chemically synthesized fiber. By supporting fibers and carbide particles, even if an oil remover is added to the liquid,
Even in the liquid, the state where the carbide particles adhere to the fiber surface is maintained. In order to support the carbide particles on the fiber more strongly,
Surfactants and organic polymer flocculants are used. As an oil removing mechanism, there is a case where oil adheres to the carbide particles carried on the fibers, and a case where oil adheres to the free carbide particles and the carbides are captured by the fibers. The amount of the carbides carried on the chemically synthesized fibers is 5 to 50 parts by weight of the dried carbides per 100 parts by weight of the chemically synthesized fibers. If the dry carbide is less than 5 parts by weight per 100 parts by weight of the chemically synthesized fiber, the oil adsorption performance will be insufficient. On the other hand, if it exceeds 50 parts by weight, it is difficult to retain the carbide on the surface of the chemically synthesized fiber, and the carbide is wasted. Furthermore, although the carbides separated from the chemically synthesized fibers adsorb the oil of the oil-containing liquid waste, it is difficult to separate the carbides that have adsorbed the oil with the chemically synthesized fibers, making it difficult to separate and remove the oil from the oil-containing liquid waste. Is.

【0009】次に、本発明の油除去剤で化学合成繊維に
炭化物を担持させるために、これらと共に使用する界面
活性剤と有機高分子凝集剤について説明する。本発明で
用いられるアニオン界面活性剤としては、パルミチン
酸、オレイン酸、ラウリン酸等の脂肪族カルボン酸やポ
リオキシエチレン鎖、ポリオキシメチレン鎖をもつアル
カリエーテルカルボン酸型アニオン界面活性剤である。
また、非イオン界面活性剤では、ポリオキシエチレン型
であるポリオキシエチレンアルキルエーテル、ポリオキ
シエチレンアルキルフェニルエーテル、ポリオキシエチ
レン脂肪酸エステル、多価アルコール系エステルエーテ
ルが好適である。多価アルコール系エステルエーテルに
は、ポリオキシエチレンソルビタンオレエートやポリオ
キシエチレンオレイン酸エステルなどである。
Next, the surfactant and the organic polymer coagulant used together with the oil removing agent of the present invention to support the carbide on the chemically synthesized fiber will be described. The anionic surfactant used in the present invention is an aliphatic carboxylic acid such as palmitic acid, oleic acid or lauric acid, or an alkali ether carboxylic acid type anionic surfactant having a polyoxyethylene chain or a polyoxymethylene chain.
Further, as the nonionic surfactant, polyoxyethylene type polyoxyethylene alkyl ether, polyoxyethylene alkylphenyl ether, polyoxyethylene fatty acid ester, and polyhydric alcohol ester ether are preferable. Examples of the polyhydric alcohol ester ether include polyoxyethylene sorbitan oleate and polyoxyethylene oleic acid ester.

【0010】本発明で用いられる高分子凝集剤は、ポリ
アクリルアミド系のアニオン系やエポキシアミン系の有
機凝結剤である分子量50万以下のカチオン系有機高分
子凝集剤、ジメチルアミノエチルメタクリレート系の両
性高分子凝集剤が、界面活性剤の代わりに界面活性剤と
同様に使用できる。化学合成繊維を界面活性剤水溶液や
界面活性剤そのものに浸漬させた後、水切り後、炭化物
を混合することにより本発明の油吸着剤を製造する。化
学合成繊維に対する界面活性剤含有量と炭化物量の比率
は、化学合成繊維100重量部に対して、界面活性剤が
1〜20重量部、炭化物が5〜50重量部である。炭化
物を50重量部以下保持するには、界面活性剤は20重
量部以下でよい。20重量部を超える界面活性剤は無駄
である。また、1重量部未満では化学合成繊維に炭化物
を保持させるのが難しい。
The polymer flocculant used in the present invention is a polyacrylamide type anion type or epoxyamine type organic coagulant, a cationic organic polymer flocculant having a molecular weight of 500,000 or less, and a dimethylaminoethylmethacrylate type amphoteric agent. Polymeric flocculants can be used as well as surfactants instead of surfactants. The chemically adsorbed fiber is immersed in a surfactant aqueous solution or the surfactant itself, drained, and then mixed with a carbide to produce the oil adsorbent of the present invention. The ratio of the surfactant content and the amount of carbide to the chemically synthesized fiber is 1 to 20 parts by weight of the surfactant and 5 to 50 parts by weight of the carbide with respect to 100 parts by weight of the chemically synthesized fiber. In order to keep 50 parts by weight or less of the carbide, the surfactant may be 20 parts by weight or less. Surfactants in excess of 20 parts by weight are wasted. Further, if it is less than 1 part by weight, it is difficult to retain the carbide in the chemically synthesized fiber.

【0011】本発明は、前記した油除去剤と含油液状廃
棄物を混合することにより、被処理物から油を分離する
含油液状廃棄物からの油の除去方法の発明である。本発
明において、含油液状廃棄物とは、下水、し尿、産業排
水等やそれらの排水処理に伴って発生する有機性汚泥や
無機性汚泥あるいは浄化槽汚泥、生ごみ、その他液状産
業廃棄物で油を含有するものである。含油液状廃棄物の
油は、動植物油、鉱物油などヘキサンで抽出される油で
ある。し尿、浄化槽汚泥、余剰汚泥などタンパク質を含
む液状廃棄物は、その中に含まれるタンパク質がヘキサ
ンで抽出されて油として測定されるので、本発明ではこ
れらのタンパク質も油に含まれる。本発明が適用できる
油の形態としては、浮上油、分散状態、乳化油、固形物
に付着した状態などである。
The present invention is an invention of a method for removing oil from an oil-containing liquid waste, in which oil is separated from an object to be treated by mixing the oil removing agent and the oil-containing liquid waste. In the present invention, the oil-containing liquid waste refers to sewage, night soil, industrial wastewater, etc. and organic sludge or inorganic sludge or septic tank sludge generated with the treatment of those wastewater, food waste, and other liquid industrial waste containing oil. It is contained. The oil of the oil-containing liquid waste is an oil extracted with hexane such as animal and vegetable oils and mineral oils. Liquid wastes containing protein such as human waste, septic tank sludge, and excess sludge are extracted from hexane as proteins contained in the liquid wastes and measured as oils. Therefore, in the present invention, these proteins are also included in oils. The form of oil to which the present invention can be applied includes floating oil, a dispersed state, an emulsified oil, and a state of being attached to a solid matter.

【0012】また、本発明は、炭化物と含油液状廃棄物
を混合した後に、化学合成繊維を添加することにより、
被処理物から油を分離する含油液状廃棄物からの油除去
方法の発明でもある。このように、含油液状廃棄物に炭
化物を粉末状又はスラリー状で添加し、混合して含油液
状廃棄物中の油を炭化物に吸着させ、油を吸着した炭化
物粒子を化学合成繊維にからめ取り、含油液状廃棄物か
ら油を除去することもできる。この方法で、炭化物の添
加率は、含油液状廃棄物スラリーあたり50〜5000
0mg/lである。浮上油には油に対して少ない炭化物
で油除去ができるが、乳化油に対しては、1%以上必要
である。油を炭化物に吸着させることから、先に炭化物
を含油液状廃棄物に添加するのが好適である。設備的に
水槽を増やすことができない場合には、炭化物と化学合
成繊維を同時に添加することもできる。
Further, according to the present invention, the chemically synthesized fiber is added after mixing the carbide and the oil-containing liquid waste,
It is also an invention of a method for removing oil from an oil-containing liquid waste that separates oil from an object to be treated. In this manner, the carbide is added to the oil-containing liquid waste in the form of powder or slurry, and the oil in the oil-containing liquid waste is adsorbed to the carbide by mixing, and the carbide particles adsorbing the oil are entangled in the chemically synthesized fiber, It is also possible to remove oil from oleaginous liquid waste. According to this method, the addition rate of carbide is 50 to 5000 per oil-containing liquid waste slurry.
It is 0 mg / l. Floating oil can remove oil with less carbide than oil, but needs 1% or more for emulsified oil. Since the oil is adsorbed on the carbide, it is preferable to add the carbide to the oil-containing liquid waste first. When it is not possible to increase the number of water tanks in terms of equipment, it is possible to simultaneously add the carbide and the chemically synthesized fiber.

【0013】さらに、本発明は、含油液状廃棄物に、前
記した油除去剤を添加混合する混合装置と、スクリーン
や脱水機で油を分離する分離装置とを有する含油液状廃
棄物からの油除去装置の発明である。本発明の油吸着剤
は、粉体であり、スラリー状又は粉体のまま含油液状廃
棄物に添加する。スラリー状にするには、工業用水や脱
水施設で容易に得られる処理水又は含油液状廃棄物その
ものに油吸着剤を添加して、既存のパルパーや機械式攪
拌機等の混合装置を用いることができる。油分離工程で
有機性の高分子凝集剤や無機性凝集剤が使用できる。
Further, according to the present invention, the oil removal from the oil-containing liquid waste has a mixing device for adding and mixing the above-mentioned oil removing agent to the oil-containing liquid waste, and a separating device for separating the oil with a screen or a dehydrator. It is the invention of the device. The oil adsorbent of the present invention is a powder, and is added to the oil-containing liquid waste as a slurry or powder. To form a slurry, an oil adsorbent can be added to industrial water, treated water easily obtained in a dehydration facility, or oil-containing liquid waste itself, and a mixing device such as an existing pulper or mechanical stirrer can be used. . Organic polymer flocculants and inorganic flocculants can be used in the oil separation step.

【0014】また、分離装置で、スクリーン分離は、ウ
エッジワイヤーやバーススクリーンなど市販のものが使
用できる。その目開きには制限が無いが、実用的な目開
きは1〜5mmである。含油液状廃棄物の汚泥濃度又は
固形物濃度が、1%以上の高濃度で、スクリーンで分離
できない場合には、市販の脱水機又は濃縮機が使用でき
る。それらはベルトプレス型やスクリュープレス型、遠
心分離、フィルタープレス型いずれも使用できる。図1
にスクリーン分離による含油液状廃棄物からの油除去の
概略図を、図2に脱水機による油除去の概略図を、図3
に炭化物粒子と化学合成繊維を別々に添加する場合の概
略図を示す。
In the separating device, a commercially available one such as a wedge wire or a bar screen can be used for screen separation. Although there is no limitation on the opening, the practical opening is 1 to 5 mm. When the sludge concentration or solid concentration of the oil-containing liquid waste is as high as 1% or more and cannot be separated by a screen, a commercially available dehydrator or concentrator can be used. A belt press type, a screw press type, a centrifugal separation, and a filter press type can be used for them. Figure 1
Fig. 3 is a schematic diagram of oil removal from oil-containing liquid waste by screen separation, and Fig. 2 is a schematic diagram of oil removal by a dehydrator.
A schematic view of the case where the carbide particles and the chemically synthesized fiber are separately added is shown in FIG.

【0015】[0015]

【実施例】以下に、本発明を実施例により具体的に説明
するが、本発明はこれらに限定されるものでない。 実施例1 合併式浄化槽汚泥100部にマヨネーズ1部とコーン油
1部をジューサーミキサーで混合したものを模擬含油液
状廃棄物とした。表1にその性状を示す。
EXAMPLES The present invention will now be described in detail with reference to examples, but the present invention is not limited thereto. Example 1 100 parts of the combined septic tank sludge and 1 part of mayonnaise and 1 part of corn oil were mixed with a juicer mixer to obtain a simulated oil-containing liquid waste. Table 1 shows its properties.

【表1】 模擬含油液状廃棄物2リットルに、長さ10mm〜15
mm、太さ約10μmのPET再生繊維(油吸着剤A)
を所定量添加し、ジューサーミキサーで300回転/分
で5分間混合し、直ちにその底部に目開き1.18mm
の金網を付けた内径100mmの円筒形容器に入れてろ
過し、分離液の流出量や分離液のヘキサン抽出物質濃度
を測定した。本発明の油吸着剤について、油吸着剤Aと
同様にB〜Eについて試験した。
[Table 1] 2 liters of simulated oil-containing liquid waste, length 10 mm ~ 15
mm recycled PET fiber with a thickness of about 10 μm (oil adsorbent A)
Was added in a predetermined amount, mixed with a juicer mixer at 300 rpm for 5 minutes, and immediately opened with 1.18 mm in the bottom.
The sample was placed in a cylindrical container having an inner diameter of 100 mm and attached with a wire net, and filtered to measure the outflow amount of the separated liquid and the hexane extract substance concentration of the separated liquid. The oil adsorbent of the present invention was tested for B to E in the same manner as the oil adsorbent A.

【0016】油吸着剤A:上記PET再生繊維 油吸着剤B:上記PET再生繊維に粒径10〜30μm
の石炭系粉末活性炭をPET再生繊維100重量部あた
り5〜20重量部担持させたもの。 油吸着剤C:上記PET再生繊維100重量部に対し
て、粒径10〜30μmの石炭系粉末活性炭と界面活性
剤ポリオキシエチレンアルキルエーテルとを5〜20重
量部ずつ担持させたもの。 油吸着剤D:油吸着剤Cの界面活性剤の代わりにアニオ
ン系高分子凝集剤を5〜20重量部使用したもの。 油吸着剤E:油吸着剤Cの界面活性剤の代わりに両性高
分子凝集剤を5〜20重量部使用したもの。 表2に実施例1の結果を示す。スクリーン分離液のヘキ
サン抽出物質の除去率から、乳化油を含む模擬含油液状
廃棄物に対しては、本発明の油吸着剤の油吸着効果が良
好であった。
Oil adsorbent A: PET regenerated fiber oil adsorbent B: PET regenerated fiber particle size 10 to 30 μm
5 to 20 parts by weight per 100 parts by weight of PET recycled fiber. Oil adsorbent C: 5 to 20 parts by weight of coal-based powdered activated carbon having a particle size of 10 to 30 μm and a surfactant polyoxyethylene alkyl ether are supported on 100 parts by weight of the PET regenerated fiber. Oil adsorbent D: 5 to 20 parts by weight of an anionic polymer flocculant is used instead of the surfactant of oil adsorbent C. Oil adsorbent E: 5 to 20 parts by weight of an amphoteric polymer coagulant is used instead of the surfactant of oil adsorbent C. Table 2 shows the results of Example 1. From the removal rate of the hexane extract substance of the screen separation liquid, the oil adsorbing effect of the oil adsorbent of the present invention was good for the simulated oil-containing liquid waste containing emulsified oil.

【0017】[0017]

【表2】 [Table 2]

【0018】比較例1 実施例1の模擬含油液状廃棄物に実施例1のPET再生
繊維や活性炭や界面活性剤や高分子凝集剤をそれぞれ添
加して実施例1と同様に実験した。表3に比較例1の結
果を示す。
Comparative Example 1 The same experiment as in Example 1 was carried out by adding the PET recycled fiber of Example 1, activated carbon, a surfactant and a polymer flocculant to the simulated oil-containing liquid waste of Example 1, respectively. Table 3 shows the results of Comparative Example 1.

【表3】 [Table 3]

【0019】実施例2 実施例1の模擬含油液状廃棄物に実施例1のPET再生
繊維や油吸着剤を添加し、カチオン系高分子凝集剤をS
Sあたり1%添加凝集後、加圧脱水試験を行った。加圧
脱水試験は、上記凝集模擬含油液状廃棄物100ミリリ
ッルを実施例1の金網で濃縮後、その濃縮汚泥を直径1
0cmの2枚のろ布にはさみ、下方を固定し上方から約
0.04MPaで2分間加圧した。脱水ケーキの含水率
とその分離液のSSとヘキサン抽出物質を測定した。実
施例1の模擬含油液状廃棄物のSSとヘキサン抽出物質
濃度からSSとヘキサン抽出物質の除去率を算出した。
表4に実施例2の結果を示す。脱水後の分離液のヘキサ
ン抽出物質濃度から乳化油を含む模擬含油液状廃棄物に
対しては、本発明の油吸着剤の油吸着効果が良好であっ
た。また、脱水ケーキの含水率から良好な脱水ができ
た。
Example 2 To the simulated oil-containing liquid waste of Example 1, the PET recycled fiber and oil adsorbent of Example 1 were added, and the cationic polymer flocculant was added to S.
After adding and coagulating 1% per S, a pressure dehydration test was conducted. In the pressure dehydration test, 100 milliliters of the above-mentioned coagulation-simulating oil-containing liquid waste was concentrated with the wire net of Example 1, and the concentrated sludge with a diameter of 1 was used.
It was sandwiched between two 0 cm filter cloths, the lower part was fixed, and pressure was applied from above for about 2 minutes at about 0.04 MPa. The water content of the dehydrated cake and the SS and hexane extracted substances of the separated liquid were measured. From the SS and hexane extract substance concentrations of the simulated oil-containing liquid waste of Example 1, the removal rates of SS and hexane extract substance were calculated.
Table 4 shows the results of Example 2. From the hexane extract substance concentration of the separated liquid after dehydration, the oil adsorption effect of the oil adsorbent of the present invention was good for the simulated oil-containing liquid waste containing the emulsified oil. In addition, good dehydration was possible based on the water content of the dehydrated cake.

【0020】[0020]

【表4】 [Table 4]

【0021】[0021]

【発明の効果】本発明は、化学合成繊維に炭化物を担持
させたり、界面活性剤や高分子凝集剤と炭化物を担持さ
せることにより、以下の効果を有する。 (1)簡便な方法で効率よく油除去が可能。 (2)乳化油に対して油除去効果が高く、後段の排水処
理への油の負荷が低減できる。 (3)分離した油の処分が容易で、作業性が向上する。
INDUSTRIAL APPLICABILITY The present invention has the following effects by supporting a carbide on a chemically synthesized fiber or by supporting a surfactant or a polymer flocculant and a carbide. (1) Oil can be removed efficiently by a simple method. (2) The oil removing effect is high with respect to the emulsified oil, and the load of the oil on the wastewater treatment in the latter stage can be reduced. (3) The separated oil is easy to dispose and the workability is improved.

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

【図1】本発明の油除去方法に用いる装置の一例を示す
概略図。
FIG. 1 is a schematic view showing an example of an apparatus used in the oil removing method of the present invention.

【図2】本発明の油除去方法に用いる装置の他の例を示
す概略図。
FIG. 2 is a schematic view showing another example of an apparatus used in the oil removing method of the present invention.

【図3】本発明の油除去方法に用いる装置の別の例を示
す概略図。
FIG. 3 is a schematic view showing another example of an apparatus used in the oil removing method of the present invention.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 化学合成繊維100重量部と、数〜10
0μmの炭化物粒子5〜50重量部とからなる油除去
剤。
1. 100 parts by weight of a chemically synthesized fiber and a few to 10 parts.
An oil remover comprising 5 to 50 parts by weight of 0 μm carbide particles.
【請求項2】 化学合成繊維100重量部と、界面活性
剤又は有機高分子凝集剤1〜20重量部と、数〜100
μmの炭化物粒子5〜50重量部とからなる油除去剤。
2. 100 parts by weight of chemically synthesized fiber, 1 to 20 parts by weight of a surfactant or an organic polymer flocculant, and a number of 100 to 100 parts.
An oil remover comprising 5 to 50 parts by weight of carbide particles having a diameter of μm.
【請求項3】 請求項1又は2記載の油除去剤と、被処
理物である含油液状廃棄物を混合することにより、被処
理物から油を分離することを特徴とする含油液状廃棄物
からの油除去方法。
3. An oil-containing liquid waste characterized by separating oil from the object to be processed by mixing the oil removing agent according to claim 1 or 2 with the oil-containing liquid waste to be processed. Oil removal method.
【請求項4】 炭化物と、被処理物である含油液状廃棄
物とを混合した後に、化学合成繊維を添加することによ
り、被処理物から油を分離することを特徴とする含油液
状廃棄物からの油除去方法。
4. An oil-containing liquid waste characterized in that oil is separated from the object to be processed by adding a chemically synthesized fiber after mixing the carbide and the oil-containing liquid waste to be processed. Oil removal method.
【請求項5】 請求項1又は2記載の油除去剤と、被処
理物である含油液状廃棄物とを混合する混合装置と、該
混合装置から油を分離する分離装置とを有することを特
徴とする含油液状廃棄物からの油除去装置。
5. A mixing device that mixes the oil removing agent according to claim 1 and the oil-containing liquid waste that is an object to be processed, and a separating device that separates oil from the mixing device. Equipment for removing oil from oil-containing liquid waste.
JP2001200864A 2001-07-02 2001-07-02 Oil removing agent and oil removing method and apparatus Pending JP2003010681A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
JP2003010681A true JP2003010681A (en) 2003-01-14

Family

ID=19037916

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006153488A (en) * 2004-11-25 2006-06-15 Canon Chemicals Inc Optical measurement method
JP2011136287A (en) * 2009-12-28 2011-07-14 Shinten Kogyo Kk Oil adsorbent and method for preserving the same
JP2016052619A (en) * 2014-09-03 2016-04-14 水ing株式会社 Method and apparatus for treating organic wastewater containing fat and oil
CN113455492A (en) * 2021-07-31 2021-10-01 河南科技大学 Biological plastify sample preparation equipment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006153488A (en) * 2004-11-25 2006-06-15 Canon Chemicals Inc Optical measurement method
JP2011136287A (en) * 2009-12-28 2011-07-14 Shinten Kogyo Kk Oil adsorbent and method for preserving the same
JP2016052619A (en) * 2014-09-03 2016-04-14 水ing株式会社 Method and apparatus for treating organic wastewater containing fat and oil
CN113455492A (en) * 2021-07-31 2021-10-01 河南科技大学 Biological plastify sample preparation equipment

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