JPH08182998A - Decompostion of fats and oils in oil-containing waste water - Google Patents

Decompostion of fats and oils in oil-containing waste water

Info

Publication number
JPH08182998A
JPH08182998A JP33766694A JP33766694A JPH08182998A JP H08182998 A JPH08182998 A JP H08182998A JP 33766694 A JP33766694 A JP 33766694A JP 33766694 A JP33766694 A JP 33766694A JP H08182998 A JPH08182998 A JP H08182998A
Authority
JP
Japan
Prior art keywords
oil
anaerobic
oils
fats
fat
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
JP33766694A
Other languages
Japanese (ja)
Inventor
Masahiro Tatara
昌浩 多田羅
Yoshitaka Togo
芳孝 東郷
Susumu Sato
佐藤  進
Kosaku Osato
幸作 大郷
Mizue Yoshida
瑞恵 吉田
Tamae Hatano
玉衣 畑野
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.)
Kajima Corp
Original Assignee
Kajima 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 Kajima Corp filed Critical Kajima Corp
Priority to JP33766694A priority Critical patent/JPH08182998A/en
Publication of JPH08182998A publication Critical patent/JPH08182998A/en
Pending legal-status Critical Current

Links

Classifications

    • Y02W10/12

Abstract

PURPOSE: To efficiently decompose fats and oils in an oil-containing waste water by anaerobically treating a digestion sludge collected from a methane fermenter in an oil- containing culture medium to separate and cultiate an anaerobic and oils decomposing bacterium and proliferating the cultivated anaerobic fats and oils decomposing bacterium in the methane fermenter into which the oil-containing waste water is to be fed. CONSTITUTION: The anaerobic fats and oils decomposing becterium is separated and cultivated by treating the digestion sludge collected from the methane fermenter 1 in the oil containing culture medium under anaerobic condition and the cultivated anaerobic fats and oils decomposing bacterium is proliferated in the methane fermenter 1 into which the oil-containing waste water is to be fed. That is, a porous granular unwoven fabric carrier on which the anaerobic fats and oils decomposing bacterium is stuck is fed to the methane fermenter 1 to form the unwoven fabric carrier layer 2. For example, a garbage raw material is fed to the methane fermenter 1 from a raw material tank 3 by using a pump 4 and is methane-fermented at about 55 deg.C while circulating the raw material in the tank by using a circulating pump 5. Since the anaerobic fats and oils decomposing bacterum is proliferated at pH 6-8, it can proliferate by only once addition to the methane fermenter 1 while treating the waste water. Accordingly, special control is unnecessary.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は各種の生活系や事業系か
ら排出される含油廃水の油脂分解処理法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for decomposing oil-containing wastewater discharged from various living and business systems.

【0002】[0002]

【従来の技術】食品工場を始め食堂や家庭からの廃水は
油脂を多量に含んでいる場合が多い。廃水中に油脂が存
在すると下水管や廃水処理施設にいろいろな問題を引き
起こすようになる。
2. Description of the Related Art Waste water from food factories, cafeterias, and households often contains a large amount of fats and oils. The presence of fats and oils in wastewater causes various problems in sewers and wastewater treatment facilities.

【0003】このため,食品工場,レストラン,ビル等
には,油脂分離施設(グリース阻集器等)が設けられ,
含油廃水から油脂の除去を行っている。油脂が除去され
た廃水は,そのまま浄化槽で処理するか,あるいは別置
の油水分離装置で更に油脂を除去した後で浄化槽で処理
している。
For this reason, oil and fat separation facilities (grease interceptors, etc.) are provided in food factories, restaurants, buildings, etc.
Oils and fats are removed from oil-containing wastewater. The wastewater from which the oils and fats have been removed is directly treated in the septic tank, or is further treated in the septic tank after the oils and fats have been further removed by a separate oil / water separator.

【0004】また,微生物を利用して含油廃水をそのま
ま好気処理する技術も開発され始めている。この方法は
従来の活性汚泥法を改良するもので,油脂を分解する微
生物を好気処理槽にあらかじめ投入しておき,ここで含
油廃水を処理するというものである。
Further, a technique for utilizing a microorganism to aerobically treat oil-containing wastewater as it is has been developed. This method is an improvement over the conventional activated sludge method, in which microorganisms that decompose fats and oils are put into an aerobic treatment tank in advance, and the oil-containing wastewater is treated there.

【0005】このような油脂分解菌には好気性菌に属す
るものと嫌気性に属するものとがあり,前者に属するも
のとして,例えばリパーゼ生産性細菌 Bacillus sp.No.
351や Pseudomonas sp.No.6が既に分離されている。
Such oil-and-fat-degrading bacteria include those belonging to aerobic bacteria and those belonging to anaerobic bacteria. As the former bacteria, for example, the lipase-producing bacterium Bacillus sp. No.
351 and Pseudomonas sp. No. 6 have already been isolated.

【0006】[0006]

【発明が解決しようとする課題】一般に油脂はボール状
に固まったり,廃水の表面に汚泥状のスカムを形成して
ポンプ場などの施設でトラブルの原因となる。従来の油
脂分離施設(グリース阻集器等)で廃水中の油脂を分離
した場合,1週間に数回は施設の清掃が必要となる。適
切な清掃を行なわないと,施設から油脂が流出する場合
もあり,環境汚染にもつながる。油脂分離装置の実際の
清掃状況の調査結果では全く清掃していない施設もあ
る。また,分離した油脂の大部分は焼却により処分する
ため,焼却のための費用も嵩むという問題がある。
Generally, fats and oils solidify into balls or form sludge-like scum on the surface of waste water, which causes troubles at facilities such as pump stations. When the oil and fat in the waste water is separated by the conventional oil and fat separation facility (grease interceptor, etc.), the facility must be cleaned several times a week. If not properly cleaned, fats and oils may leak from the facility, leading to environmental pollution. Some facilities did not clean at all based on the survey results of the actual cleaning status of the oil and fat separation device. Further, since most of the separated oils and fats are disposed of by incineration, there is a problem that the cost for incineration increases.

【0007】活性汚泥法の改良法である好気処理で含油
廃水を処理する方法は,油脂濃度が100mg/リット
ル以上になると活性汚泥処理が難しくなるといわれてい
る。すなわち,油脂を槽内に均一に懸濁することが難し
く,油脂濃度の上昇に伴って処理能力が低下するので,
高濃度に油脂を含む廃水に適用するのは難しいという問
題がある。また,好気処理により含油廃水を処理する場
合には油脂を均一に懸濁することが難しく,油脂濃度の
上昇に伴って処理能力が低下するし,その原理は従来の
活性汚泥処理と同様であるから,曝気動力等のエネルギ
ー消費が大きいことや,余剰汚泥が出る等の問題もあ
る。
In the method of treating oil-containing wastewater by aerobic treatment, which is an improved method of the activated sludge method, it is said that the activated sludge treatment becomes difficult when the fat and oil concentration becomes 100 mg / liter or more. In other words, it is difficult to evenly suspend the fats and oils in the tank, and as the concentration of fats and oils increases, the processing capacity decreases.
There is a problem that it is difficult to apply to wastewater containing oil and fat at a high concentration. In addition, when treating oil-containing wastewater by aerobic treatment, it is difficult to uniformly suspend fats and oils, and the treatment capacity decreases as the concentration of fats and oils increases. The principle is the same as in conventional activated sludge treatment. Therefore, there are problems that energy consumption such as aeration power is large and that excess sludge is generated.

【0008】このように,従来の含油廃水の油脂処理に
は,メンテナンス,処理方法,処理能力等の点で種々の
問題があった。本発明はこのようなやっかいな問題を解
決しようとするものである。
As described above, the conventional fat and oil treatment of oil-containing wastewater has various problems in terms of maintenance, treatment method, treatment capacity and the like. The present invention is intended to solve such a troublesome problem.

【0009】[0009]

【課題を解決するための手段】本発明によれば,メタン
発酵槽から採取した消化汚泥を含油培地で嫌気条件下で
処理して嫌気性油脂分解菌を分離培養し,培養された嫌
気性油脂分解菌を含油廃水が投入されるメタン発酵槽で
増殖させることを特徴とする含油廃水の油脂分解方法を
提供する。ここで,含油廃水を投入するメタン発酵槽に
は,粒状の不織布担体を液面に浮遊させておくのがよ
い。
According to the present invention, digested sludge collected from a methane fermentation tank is treated in an oil-containing medium under anaerobic conditions to separate and cultivate anaerobic oil-degrading bacteria, and the cultured anaerobic oil and fat. Provided is a method for decomposing fats and oils of oil-containing wastewater, which comprises proliferating degrading bacteria in a methane fermentation tank into which oil-containing wastewater is charged. Here, in the methane fermentation tank into which the oil-containing wastewater is charged, it is preferable to suspend the granular non-woven fabric carrier on the liquid surface.

【0010】[0010]

【作用】厨芥処理に供される通常のメタン発酵槽の消化
汚泥には,嫌気性油脂分解菌も生息している。この嫌気
性油脂分解菌は適切な含油培地で嫌気条件下で処理する
と分離培養することができる。この嫌気性油脂分解菌を
メタン発酵槽内で含油廃水を投入しながら増殖させれ
ば,投入された含油廃水は分解処理され,その油脂分を
効率よく除去できる。
[Function] Anaerobic fat-and-oil-degrading bacteria also inhabit the digested sludge of a normal methane fermentation tank used for garbage treatment. This anaerobic oil-degrading bacterium can be separated and cultured by treating it with an appropriate oil-containing medium under anaerobic conditions. If the anaerobic oil-degrading bacteria are grown in a methane fermentation tank while the oil-containing wastewater is being added, the input oil-containing wastewater is decomposed and the oil and fat components can be efficiently removed.

【0011】この嫌気性油脂分解菌はpH6〜8の間で
増殖するので,メタン発酵槽に一度添加するだけで廃水
を処理しながら増殖する。そのため,特別の管理は必要
とはせず通常のメタン発酵同様なメンテナンスだけで済
むし,好気処理のように曝気動力は必要なく余剰汚泥排
出量も少ない。更に,エネルギー源としてのメタンガス
を回収できるので経済性にも優れる。
Since the anaerobic fat-and-oil-degrading bacteria grow at a pH of 6 to 8, the anaerobic fat-and-oil decomposing bacteria grow while treating the wastewater by adding it once to the methane fermentation tank. Therefore, no special management is required, and only maintenance similar to normal methane fermentation is required. Aeration power is not required unlike aerobic treatment, and excess sludge emissions are small. In addition, it is economical because it can recover methane gas as an energy source.

【0012】本発明の実施にさいし,多孔質で粒状の不
織布担体をメタン発酵槽の液面に浮遊させておくと,含
油廃水中の油脂分は処理槽の液面近くに浮遊する性質が
あるので,この液面近くの油脂分と不織布担体に付着し
た嫌気性油脂分解菌との接触機会が多くなり,この多孔
質担体を媒介として嫌気性油脂分解菌の増殖活動が盛ん
になり,油脂の分解が一層効率よく進行し,高濃度に油
脂を含む含油廃水でも簡易に処理できる。
In carrying out the present invention, when a porous and granular non-woven fabric carrier is floated on the liquid surface of a methane fermentation tank, the oil and fat in the oil-containing wastewater has a property of floating near the liquid surface of the treatment tank. Therefore, the chances of contact between the oil and fat near the liquid surface and the anaerobic fat-decomposing bacteria adhering to the non-woven fabric carrier increase, and the proliferative activity of the anaerobic fat-decomposing bacteria becomes active through this porous carrier, and Decomposition proceeds more efficiently, and oil-containing wastewater containing oil and fat at high concentration can be easily treated.

【0013】多孔質粒状の不織布担体としては,ガラス
繊維またはプラスチックス繊維で構成された多孔性シー
トを軽量プラスチックスの粒状体(好ましくは直径5〜
60mmの粒状体)の周囲に被せたものが好適であり,
これを,槽内の液面を1段以上で覆うに十分な数量で浮
遊させる。ガラス繊維やプラスチックス繊維からなる多
孔性シート(不織布)は微生物固定能力が高く,これに
固定された油脂分解菌は流出する恐れがない。そして,
中空プラスチック,プラスチック発泡体等の軽量の粒状
プラスチックスを,該多孔性シートを保持させるための
芯材として用いることによって,この不織布担体を自由
に槽内に流動浮遊させることができると共に,この芯材
としてのプラスチックスも微生物担体として機能する。
As the porous granular nonwoven fabric carrier, a porous sheet composed of glass fiber or plastics fiber is used as a lightweight plastics granular body (preferably having a diameter of 5 to 5).
It is preferable to cover it around a 60 mm granular body,
Float this in sufficient quantity to cover the liquid level in the tank with one or more steps. The porous sheet (nonwoven fabric) made of glass fiber or plastics fiber has a high ability to fix microorganisms, and there is no risk that oil-degrading bacteria fixed to this will flow out. And
By using lightweight granular plastics such as hollow plastics and plastic foams as the core material for holding the porous sheet, the nonwoven fabric carrier can be freely flown and suspended in the tank and the cores Plastics as a material also functions as a microorganism carrier.

【0014】[0014]

【実施例】【Example】

【0015】以下の実施例において,廃水の成分の分析
は工業廃水試験法(JIS K 0102)に準じた。
In the following examples, the analysis of the components of waste water was based on the Industrial Waste Water Test Method (JIS K 0102).

【0016】〔実施例1〕厨芥処理後の高温メタン発酵
汚泥を0.5ml(ミリリットル,以下同じ)採取し,
表1に示す培地100mlに接種した。この培地はオー
トクレープにより120℃×20分間滅菌したあとで使
用した。培養には嫌気ジャーファーメンタを用いて55
℃で2週間培養した。なおメタン発酵槽内と同様の雰囲
気下で培養するため,気層にはCH4:CO2=7:3の
ガスを通気しながら培養した。
[Example 1] 0.5 ml (milliliter, the same applies hereinafter) of high temperature methane fermented sludge after garbage treatment was sampled,
100 ml of the medium shown in Table 1 was inoculated. This medium was used after being sterilized by an autoclave at 120 ° C. for 20 minutes. For culturing, use an anaerobic jar fermenter 55
The cells were cultured at 0 ° C for 2 weeks. Since the culture was carried out in the same atmosphere as in the methane fermentation tank, the gas layer was cultivated while aeration of gas of CH 4 : CO 2 = 7: 3.

【0017】この培養処理後,培養液0.5mlを表2
に示す培地100mlに接種し,油脂分解能の有無につ
いてテストした。油脂分解能については,n−ヘキサン
抽出物の経時変化を指標として用いた。その結果を図1
に示した。
After this culture treatment, 0.5 ml of the culture solution was added to Table 2.
The medium was inoculated into 100 ml of the medium shown in, and tested for the presence or absence of oil and fat degrading. Regarding the oil and fat degradability, the change with time of the n-hexane extract was used as an index. The result is shown in Figure 1.
It was shown to.

【0018】[0018]

【表1】 [Table 1]

【0019】[0019]

【表2】 [Table 2]

【0020】図1に見られるように,n−ヘキサン抽出
物は,嫌気性油脂分解菌を接種後,徐々に減少し,2週
間後には嫌気性油脂分解菌接種前の10%以下となっ
た。この結果から,本方法で分離した嫌気性油脂分解菌
は,油脂を90%以上除去できたと考えられる。
As shown in FIG. 1, the n-hexane extract gradually decreased after inoculation with the anaerobic oil and fat decomposing bacteria, and was reduced to 10% or less 2 weeks after the inoculation with the anaerobic oil and fat decomposing bacteria. . From this result, it is considered that the anaerobic oil-and-fat-decomposing bacteria separated by this method were able to remove the oil and fat by 90% or more.

【0021】〔実施例2〕実施例1で分離した嫌気性油
脂分解菌を前記同様の表2の培地に接種し,55℃で増
殖させ,菌濃度が1×108cells/mlとなった
ところで,直径2cmの不織布担体を投入し,さらに2
週間培養して,該担体に嫌気性油脂分解菌を付着させ
た。この不織布担体は中空の樹脂球の周囲にガラス繊維
からなる不織布シートを被着させたものである。
[Example 2] The anaerobic fat-and-oil-degrading bacteria isolated in Example 1 were inoculated into the same medium shown in Table 2 above and grown at 55 ° C to give a bacterial concentration of 1 x 10 8 cells / ml. By the way, we put in a non-woven fabric carrier with a diameter of 2 cm, and
After culturing for a week, anaerobic fat and oil decomposing bacteria were attached to the carrier. This non-woven fabric carrier is one in which a non-woven fabric sheet made of glass fiber is adhered around hollow resin balls.

【0022】このようにして嫌気性油脂分解菌を付着さ
せた不織布担体を,図2に示すように,メタン発酵槽1
内に投入した。図中の2はこの不織布担体層を示す。メ
タン発酵槽内での不織布担体投入時の嫌気性油脂分解菌
濃度は5×108cells/ml程度であった。
The non-woven fabric carrier to which the anaerobic fat-and-oil-degrading bacteria have been attached in this manner is shown in FIG.
I put it in. Reference numeral 2 in the figure denotes this nonwoven fabric carrier layer. The concentration of the anaerobic fat-and-oil-degrading bacteria at the time of adding the non-woven fabric carrier in the methane fermentation tank was about 5 × 10 8 cells / ml.

【0023】メタン発酵槽1では,表3に示すような組
成の厨芥原料を原料槽3からポンプ4によって投入し,
循環ポンプ5によって槽内原料を循環しながら,滞留時
間6日となるように55℃でメタン発酵を行った。な
お,メタン発酵槽1の消化ガスライン6には脱硫装置7
およびガスメーター8が取り付けられている。
In the methane fermentation tank 1, the kitchen waste material having the composition shown in Table 3 is charged from the raw material tank 3 by the pump 4.
While circulating the raw materials in the tank by the circulation pump 5, methane fermentation was performed at 55 ° C. so that the residence time was 6 days. In addition, the desulfurization device 7 is installed in the digestion gas line 6 of the methane fermentation tank 1.
And a gas meter 8 is attached.

【0024】[0024]

【表3】 [Table 3]

【0025】この連続処理において,担体2を投入後,
メタン発酵槽から発酵液のサンプルを採取してn−ヘキ
サン抽出物量を測定し,その経時変化を調べた。その結
果を図3に示した。図3に見られるように,n−ヘキサ
ン抽出物量は,担体2の投入後徐々に減少し,10日間
培養後からは厨芥原水の10%以下となった。このこと
から,本方法で分離した油脂分解菌は,メタン発酵槽に
投入するだけで,高効率に厨芥中の油脂を分解できるこ
とがわかった。また,連続的に廃水を処理する際にも,
集積培養した嫌気性油脂分解菌を一度投入すれば,連続
的に油脂を分解できることもわかった。
In this continuous process, after the carrier 2 is charged,
A sample of the fermentation broth was taken from the methane fermentation tank, the amount of n-hexane extract was measured, and its change over time was examined. The results are shown in Fig. 3. As can be seen in FIG. 3, the amount of n-hexane extract gradually decreased after the carrier 2 was added, and became 10% or less of the garbage raw water after the culture for 10 days. From this, it was found that the oil-and-fat-decomposing bacteria separated by this method can decompose the oil and fat in the kitchen waste with high efficiency simply by introducing it into the methane fermentation tank. Also, when treating wastewater continuously,
It was also found that the fat and oil can be continuously decomposed by adding the anaerobic fat and oil-degrading bacteria that have been accumulated and cultured once.

【0026】〔実施例3〕表4に示す組成の食品工場排
出スカムを実施例2と同様に連続処理した。すなわち,
嫌気性油脂分解菌を付着させた不織布担体2をメタン発
酵槽1内に充填し嫌気性油脂分解菌濃度を約5×108
celles/mlとした。メタン発酵は該スカムを滞
留時間6日となるように供給し,55℃で行った。
Example 3 The scum discharged from a food factory having the composition shown in Table 4 was continuously treated in the same manner as in Example 2. That is,
The methane fermentation tank 1 is filled with the non-woven fabric carrier 2 to which the anaerobic fat and oil decomposing bacteria are attached, and the concentration of the anaerobic fat and oil decomposing bacteria is about 5 × 10 8.
cells / ml. The methane fermentation was performed at 55 ° C. by supplying the scum so that the residence time was 6 days.

【0027】実施例2と同様にn−ヘキサン抽出物量の
経時変化を指標として油脂分解能を調べた。その結果を
図4に示した。図4に見られるように,n−ヘキサン抽
出物は,嫌気性油脂分解菌接種後減少し,5日間培養後
からは原水の10%以下となった。このことから,本方
法で分離した油脂分解菌は,メタン発酵槽に投入するだ
けで,高効率にスカム中の油脂を分解できることがわか
った。また,連続的に廃水を処理する際にも,集積培養
した嫌気性油脂分解菌を一度投入すれば,連続的に油脂
を分解できることもわかった。
In the same manner as in Example 2, the ability to decompose fats and oils was examined using the change over time in the amount of n-hexane extract as an index. The results are shown in Fig. 4. As shown in FIG. 4, the amount of n-hexane extract decreased after inoculation of the anaerobic fat and oil degrading bacteria, and became 10% or less of the raw water after 5 days of culture. From this, it was found that the oil-and-fat-decomposing bacteria separated by this method can decompose the oil and fat in scum with high efficiency simply by adding it to the methane fermentation tank. It was also found that even when treating wastewater continuously, if the anaerobic fat-degrading bacteria that had been subjected to concentrated culture were added once, the fats and oils could be continuously decomposed.

【0028】なお,これらの実施例では高温メタン発酵
汚泥より嫌気性油脂分解菌を分離した例を示したが,高
温メタン発酵汚泥に限らず,中温または低温メタン発酵
汚泥からも嫌気性油脂分解菌を同様の方法で分離するこ
とができ,この分離した嫌気性油脂分解菌も前記実施例
同様に含油廃水の処理に利用できる。
In these examples, the anaerobic oil-degrading bacteria were separated from the high-temperature methane-fermenting sludge, but not limited to the high-temperature methane-fermenting sludge, the anaerobic oil-degrading bacteria can also be extracted from the medium-temperature or low-temperature methane-fermenting sludge. Can be separated by the same method, and the separated anaerobic oil-degrading bacterium can be used for treating oil-containing wastewater as in the above-mentioned Examples.

【0029】[0029]

【発明の効果】以上説明したように,本方法により分離
した油脂分解菌を用いて含油廃水の処理を行うと,次の
ような効果がある。 (1) グリース阻集器等の油脂分離施設を設けなくてよ
い。 (2) メタン発酵槽に含油廃水を投入するだけで油脂が分
解するので既存のメタン発酵装置でも本発明に適用で
き,新たな設備投資の必要がない。 (3) 新たに廃水処理装置を設置する場合もメタン発酵装
置のみでよいので省スペース,経済性に優れる。 (4) 本発明の処理は好気処理とは異なって嫌気処理であ
るから,曝気動力などが必要なく,また余剰汚泥が出な
いためにランニングコストが安い。 (5) 一度投入した嫌気性油脂分解菌はメタン発酵槽内で
増殖するため,特別のメンテナンスを必要としない。
As described above, when the oil-containing wastewater is treated by using the oil-and-fat-degrading bacteria separated by this method, the following effects are obtained. (1) It is not necessary to provide an oil separation facility such as a grease interceptor. (2) Since oils and fats are decomposed simply by adding oil-containing wastewater to the methane fermentation tank, the existing methane fermentation apparatus can be applied to the present invention, and new capital investment is not required. (3) Even if a new wastewater treatment device is installed, only the methane fermentation device is required, so it is space-saving and economical. (4) Unlike the aerobic treatment, the treatment of the present invention is an anaerobic treatment, so that aeration power or the like is not necessary and no running sludge is generated, so the running cost is low. (5) Since the anaerobic fat-and-oil-degrading bacteria once added grow in the methane fermentation tank, no special maintenance is required.

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

【図1】厨芥の高温メタン発酵槽から採取した嫌気性油
脂分解菌の油脂分解能を示すグラフである。
FIG. 1 is a graph showing the oil and fat decomposing ability of anaerobic oil and fat decomposing bacteria collected from a high temperature methane fermentation tank of kitchen waste.

【図2】嫌気性油脂分解菌を用いて油脂を連続分解する
のに使用した装置の略断面機器配置図である。
FIG. 2 is a schematic cross-sectional device layout diagram of an apparatus used for continuously decomposing oils and fats using anaerobic oil and fat decomposing bacteria.

【図3】図2の装置で含油廃水を連続処理した場合の油
脂除去率の経時変化を示す図である。
FIG. 3 is a diagram showing a change with time of an oil and fat removal rate when oil-containing wastewater is continuously treated by the apparatus of FIG.

【図4】図2の装置で食品工場排出スカムを連続処理し
た場合の油脂除去率の経時変化を示す図である。
FIG. 4 is a diagram showing a change over time in the oil and fat removal rate when the scum discharged from a food factory is continuously treated by the apparatus of FIG.

【符号の説明】[Explanation of symbols]

1 メタン発酵槽 2 多孔質粒状の不織布担体充填層 3 原水タンク 4 ポンプ 5 循環ポンプ 6 メタン分解槽 7 脱硫装置 8 ガスメーター 1 methane fermentation tank 2 porous granular non-woven fabric carrier packed bed 3 raw water tank 4 pump 5 circulation pump 6 methane decomposition tank 7 desulfurization device 8 gas meter

【表4】 [Table 4]

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大郷 幸作 東京都調布市飛田給二丁目19番1号 鹿島 建設株式会社技術研究所内 (72)発明者 吉田 瑞恵 東京都調布市飛田給二丁目19番1号 鹿島 建設株式会社技術研究所内 (72)発明者 畑野 玉衣 東京都調布市飛田給二丁目19番1号 鹿島 建設株式会社技術研究所内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Kosaku Osato 2-19-1 Tobita-yari, Chofu-shi, Tokyo Kashima Construction Co., Ltd. Technical Research Institute (72) Inventor Mizue Yoshida 2-1-1-1, Tobita, Chofu-shi, Tokyo Kashima Construction Co., Ltd. Technical Research Institute (72) Inventor Tamano Hatano 2-1-1, Tobita, Chofu-shi, Tokyo Kashima Construction Co., Ltd. Technical Research Institute

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 メタン発酵槽から採取した消化汚泥を含
油培地で嫌気条件下で処理して嫌気性油脂分解菌を分離
培養し,培養された嫌気性油脂分解菌を含油廃水が投入
されるメタン発酵槽で増殖させることを特徴とする含油
廃水の油脂分解方法。
1. Methane into which digested sludge collected from a methane fermentation tank is treated in an oil-containing medium under anaerobic conditions to separate and cultivate anaerobic fat-and-oil-degrading bacteria, and oil-containing wastewater is added to the cultured anaerobic fat-and-oil-degrading bacteria. A method for decomposing fats and oils containing oil-containing wastewater, the method comprising proliferating in a fermenter.
【請求項2】 含油廃水が投入されるメタン発酵槽に
は,多孔質で粒状の不織布担体が液面に浮遊させてある
請求項1に記載の含油廃水の油脂分解法。
2. The method of decomposing oil-containing wastewater according to claim 1, wherein a porous granular granular non-woven fabric carrier is suspended on the liquid surface in the methane fermentation tank into which the oil-containing wastewater is charged.
JP33766694A 1994-12-28 1994-12-28 Decompostion of fats and oils in oil-containing waste water Pending JPH08182998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33766694A JPH08182998A (en) 1994-12-28 1994-12-28 Decompostion of fats and oils in oil-containing waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33766694A JPH08182998A (en) 1994-12-28 1994-12-28 Decompostion of fats and oils in oil-containing waste water

Publications (1)

Publication Number Publication Date
JPH08182998A true JPH08182998A (en) 1996-07-16

Family

ID=18310815

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33766694A Pending JPH08182998A (en) 1994-12-28 1994-12-28 Decompostion of fats and oils in oil-containing waste water

Country Status (1)

Country Link
JP (1) JPH08182998A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000271593A (en) * 1999-03-24 2000-10-03 Ebara Corp Anaerobic treatment method of grease-containing waste water
JP2000271592A (en) * 1999-03-24 2000-10-03 Ebara Corp Anaerobic treatment method of grease-containing waste water
JP2001017989A (en) * 1999-07-07 2001-01-23 Ebara Corp Anaerobic treatment of oil and fat-containing waste water or oil and fat-containing sludge
JP2001017990A (en) * 1999-07-07 2001-01-23 Ebara Corp Anaerobic treatment of oil and fat-containing waste water
JP2001129580A (en) * 1999-11-02 2001-05-15 Kl Plant Kk Apparatus for treating waste water containing oil and fat
JP2001321792A (en) * 2000-03-08 2001-11-20 Japanese Research & Development Association For Environment-Friendly Processing In Food Industry Method and system for anaerobically treating grease pollutant
JP2016007574A (en) * 2014-06-24 2016-01-18 オルガノ株式会社 Anaerobic biological treatment device and anaerobic biological treatment method
JP2018149513A (en) * 2017-03-14 2018-09-27 住友重機械工業株式会社 Oil and fat-containing wastewater treatment apparatus

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000271593A (en) * 1999-03-24 2000-10-03 Ebara Corp Anaerobic treatment method of grease-containing waste water
JP2000271592A (en) * 1999-03-24 2000-10-03 Ebara Corp Anaerobic treatment method of grease-containing waste water
JP2001017989A (en) * 1999-07-07 2001-01-23 Ebara Corp Anaerobic treatment of oil and fat-containing waste water or oil and fat-containing sludge
JP2001017990A (en) * 1999-07-07 2001-01-23 Ebara Corp Anaerobic treatment of oil and fat-containing waste water
JP2001129580A (en) * 1999-11-02 2001-05-15 Kl Plant Kk Apparatus for treating waste water containing oil and fat
JP2001321792A (en) * 2000-03-08 2001-11-20 Japanese Research & Development Association For Environment-Friendly Processing In Food Industry Method and system for anaerobically treating grease pollutant
JP2016007574A (en) * 2014-06-24 2016-01-18 オルガノ株式会社 Anaerobic biological treatment device and anaerobic biological treatment method
JP2018149513A (en) * 2017-03-14 2018-09-27 住友重機械工業株式会社 Oil and fat-containing wastewater treatment apparatus

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