JPH07982A - Waste water treatment - Google Patents

Waste water treatment

Info

Publication number
JPH07982A
JPH07982A JP5179735A JP17973593A JPH07982A JP H07982 A JPH07982 A JP H07982A JP 5179735 A JP5179735 A JP 5179735A JP 17973593 A JP17973593 A JP 17973593A JP H07982 A JPH07982 A JP H07982A
Authority
JP
Japan
Prior art keywords
sludge
wastewater
treatment
waste water
conventional method
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
JP5179735A
Other languages
Japanese (ja)
Inventor
Kiyoshi Eguchi
澄 江口
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP5179735A priority Critical patent/JPH07982A/en
Publication of JPH07982A publication Critical patent/JPH07982A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Treatment Of Biological Wastes In General (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To stabilize the treatment, to decrease the formed quantity of excess sludge, besides to save labor, to save resources and to save energy in biological treatment of waste water. CONSTITUTION:This is a method for treating waste water where an extract extracted from natural citrus fruits is added during a process for biologically treating waste water. The action of microorganisms participating in the purification of waste water is improved by the addition of the extract to form activated sludge rich in sedimentation property and concentration property. In this way, the effect of solid-liquid separation is increased to stabilize the treatment and the deterioration of the quality of the treated water due to sludge outflow is prevented and also the generated quantity of excessive sludge is decreased.

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、排水の浄化に関与する
生物の活動を活性化させて、排水を処理する方法に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating wastewater by activating the activities of organisms involved in the purification of wastewater.

【0002】[0002]

【従来の技術】有機性排水を浄化処理する場合、微生物
を一定の条件のもとで繁殖させて、自然界で行なわれて
いる浄化作用を、短期的に達成させる生物学的処理方法
が広く採用されており、活性汚泥法はその代表的な処理
方法である。排水中には細菌やその他の生物が自然に発
生する。この細菌は排水中に空気を吹き込むなどによる
酸素の存在のもとで、周囲の排水中の有機物をとって発
育、繁殖し、微細な塊を形成する。この塊の周囲にはさ
まざまな好気性微生物が付着し、この微生物も排水中の
微細な浮遊物や溶解性物質や細菌を食物として摂り入れ
て繁殖する。かくして、排水中には多数の微生物の塊を
生ずるが、これは綿屑状を呈し、フロックと呼ばれる。
つまり、排水中の有機性汚染物質は微生物の働きによっ
てフロックに変わり、その結果、排水はフロックときれ
いな水に分かれることになる。このフロックは一般に水
より重いので、フロックの混合液を静置するとフロック
は沈殿して、きれいな上澄水が処理水として得られる。
沈殿したフックは汚泥を形成するが、この汚泥は要する
に生物の集積であり、普通の汚泥と異なり一種の生きも
のである。よって、この汚泥をとくに活性汚泥という。
この汚泥を再び排水中に戻し、適度な酸素の存在のもと
で排水と混合、接触させると汚染物質を食物として摂
り、汚染物質の除去に働く。再び排水中に戻す活性汚泥
を返送汚泥と呼ぶ。以上が、好気性生物学的処理方法に
よる排水の処理原理であり、返送汚泥を利用する処理方
法が活性汚泥法である。活性汚泥法による排水処理施設
は、一般に、排水と活性汚泥および酸素との混合、接触
によって排水中の有機汚染物質の生物分解を行なうばっ
気槽と、その結果として生成される汚泥と上澄水の分離
を行なう沈殿槽とで構成される。活性汚泥法は、有機性
排水を高度に処理する場合、生物学的処理方法のうち最
も優れた処理方法の一つであるが、この方法には次のよ
うな宿命的欠点を有している。すなわち、急激なショッ
クや負荷条件の変化による、活性汚泥の沈降性の悪化や
沈殿槽内で汚泥が浮上し、放流水に混入して流出するこ
とによる処理水水質の悪化であり、維持管理の大半は汚
泥管理に費やされるといっても過言ではない。とくに活
性汚泥の膨化は、しばしば予期せぬときに起こり、処理
機能に致命的悪影響を与える。活性汚泥法では、ばっ気
槽における生物分解がいかに優れていても、沈殿槽にお
ける固液分離が不良であれば、放流水中に汚泥の流出が
多くなり、処理水の水質悪化はさけられない。さらに、
沈殿汚泥の濃縮が良好に行なわれなくなり、返送汚泥の
濃度が薄くなって、ばっ気槽内の活性汚泥濃度が低くな
り、排水処理有用微生物の保持ができなくなって生物分
解が低下する。したがって、沈殿槽における固液分離の
良否は排水の浄化度に極めて大きな影響をおよぼす。こ
のような汚泥の流出による処理水水質の悪化対策とし
て、従来は、ばっ気槽や沈殿槽に凝集剤を添加して汚泥
の沈降性を高めるとか、沈殿槽の増設やろ過装置等の設
置によって、流出する汚泥を捕捉するなどの対症療法的
方法が採用されていた。さらに、活性汚泥法を維持して
いく上で大きな欠点は、余剰汚泥の発生量が多いことで
ある。余剰汚泥は排水の生物学的処理では必然的に発生
するもので、返送汚泥として利用される残余の汚泥であ
る。この汚泥は含水率が高く、かつ、濃縮性と脱水性が
悪いという性質があり、余剰汚泥の処分費は排水処理に
要する総費用の約半を占めているのが実情である。さら
に、この汚泥は、腐敗し易く悪臭や衛生害虫発生等の公
害を引き起こす原因となる。余剰汚泥は水分の含有量に
よって、その容量は著しく左右される。例えば、水分含
量99%の汚泥が濃縮(脱水)され、水分含量が98%
になったとすれば、容量は当初のそれの二分の一に減少
する。したがって、濃縮性に富み、かつ、含水率の低い
余剰汚泥を得ることは、余剰汚泥の処分費を節減する上
から極めて重要である。微生物活動を活性化して余剰汚
泥を減少させる処理方法として、ばっ気槽内にバクテリ
ヤ等の微生物製剤や特公昭63−65396号公報に記
載されいてる微生物活性助剤を投与するなどの方法があ
る。活性汚泥法等の生物学的処理法は、その系に自然発
生的に増殖した多種多様の昆合培養系の微生物を利用し
て、種々雑多な成分を含む、きわめて複雑な多成分系の
排水を処理するために、系内の微生物の優占種は排水の
基質やその他の処理条件によって変化する。したがっ
て、微生物製剤を投与することによって、系内の生物相
を制御することは事実上不可能であり、その効果は期待
できなかった。また、特公昭63−65396号公報に
記載されている、微生物活性助剤を投与する方法は、チ
リー、ボリビア、ペルー等に自生している特殊な植物
(シャボンの木)から抽出した、有効主成分がサポニン
であると考えられる抽出物(シャボン液)を投与する方
法である。この方法は各種排水処理分野において採用さ
れて、その有効性が認められているが、水産加工工場の
排水処理に使用した実施報告例「PPM、第18巻第1
2号(日本工業新聞社発行)」では、この抽出物は高価
であるために、添加に要した費用は排水処理に要した総
処理費用の約30%を占めており、実施前と比較して約
4%節減されたにすぎず、顕著な経済効果は出ていな
い。
2. Description of the Related Art When purifying organic waste water, a biological treatment method is widely adopted in which microorganisms are propagated under certain conditions to achieve a purifying action performed in nature in a short period of time. The activated sludge method is a typical treatment method. Bacteria and other organisms naturally occur in the wastewater. In the presence of oxygen by blowing air into the wastewater, this bacterium takes up organic matter in the surrounding wastewater, grows and reproduces, and forms a fine lump. Various aerobic microorganisms adhere to the surroundings of this lump, and these microorganisms also ingest fine suspended matter, soluble substances and bacteria in the wastewater as foods and propagate. Thus, a large number of microbial clumps are formed in the wastewater, which are cotton dust-like and are called flocs.
In other words, the organic pollutants in the wastewater turn into flocs by the action of microorganisms, and as a result, the wastewater is divided into flocs and clean water. Since this floc is generally heavier than water, when the mixed solution of flocs is left to stand, the flocs precipitate and clean supernatant water is obtained as treated water.
The settled hooks form sludge, which is essentially an accumulation of organisms and is a kind of living thing unlike ordinary sludge. Therefore, this sludge is particularly called activated sludge.
When this sludge is returned to the wastewater and mixed and contacted with the wastewater in the presence of an appropriate amount of oxygen, the pollutants are taken as food and work to remove the pollutants. The activated sludge that is returned to the wastewater is called return sludge. The above is the treatment principle of wastewater by the aerobic biological treatment method, and the treatment method using returned sludge is the activated sludge method. Wastewater treatment facilities using the activated sludge method generally have an aeration tank that biodegrades organic pollutants in the wastewater by mixing and contacting the wastewater with the activated sludge and oxygen, and the resulting sludge and supernatant water. It consists of a settling tank for separation. The activated sludge method is one of the most excellent biological treatment methods for highly treating organic wastewater, but it has the following fatal drawbacks. . That is, the deterioration of the settling property of activated sludge due to sudden shocks and changes in load conditions, and the deterioration of the treated water quality due to the sludge floating in the settling tank and being mixed with the discharged water and flowing out. It is no exaggeration to say that most of the money is spent on sludge management. In particular, the swelling of activated sludge often occurs at an unexpected time and has a fatal adverse effect on the treatment function. In the activated sludge method, no matter how excellent the biodegradation in the aeration tank is, if the solid-liquid separation in the sedimentation tank is poor, the sludge will flow out into the discharged water a lot and the water quality of the treated water will not deteriorate. further,
Concentration of the settled sludge will not be carried out well, the concentration of the returned sludge will be low, the concentration of activated sludge in the aeration tank will be low, and it will not be possible to retain useful microorganisms for wastewater treatment, and biodegradation will be reduced. Therefore, the quality of solid-liquid separation in the settling tank has a great influence on the degree of purification of wastewater. As measures against the deterioration of treated water quality due to such sludge outflow, conventionally, coagulants have been added to aeration tanks or settling tanks to increase sludge settling ability, or additional settling tanks or filtration devices have been installed. , Symptomatic treatment methods such as capturing the sludge that had flowed out were adopted. Further, a major drawback in maintaining the activated sludge method is that a large amount of surplus sludge is generated. Excess sludge is inevitably generated in biological treatment of wastewater, and is the residual sludge used as return sludge. This sludge has a high water content and poor concentration and dewatering properties, and the actual disposal cost of surplus sludge accounts for about half of the total cost required for wastewater treatment. Furthermore, this sludge easily decomposes and causes pollution such as offensive odors and hygienic pests. The volume of excess sludge greatly depends on the water content. For example, sludge with a water content of 99% is concentrated (dehydrated) and the water content is 98%.
If so, the capacity would be reduced to one half of that originally. Therefore, it is extremely important to obtain surplus sludge that is highly concentrated and has a low water content in order to reduce the disposal cost of surplus sludge. As a treatment method for activating microbial activity to reduce excess sludge, there is a method of administering a microbial agent such as bacteria or a microbial activity aid described in JP-B-63-65396 into an aeration tank. Biological treatment methods such as the activated sludge method utilize a wide variety of microorganisms in the Kunming culture system that spontaneously grew in the system, and it is an extremely complicated multi-component wastewater containing various components. In order to treat wastewater, the predominant species of microorganisms in the system vary depending on the wastewater substrate and other treatment conditions. Therefore, it is virtually impossible to control the biota in the system by administering the microbial agent, and its effect could not be expected. In addition, the method of administering a microbial activation aid described in JP-B-63-65396 is an effective main ingredient extracted from a special plant (soap tree) that grows naturally in Chile, Bolivia, Peru, etc. It is a method of administering an extract (soap solution) thought to be a saponin as a component. This method has been adopted in various fields of wastewater treatment and its effectiveness has been recognized, but an implementation report example “PPM, Vol.
No. 2 (published by Nihon Kogyo Shimbun) ”, this extract is expensive, so the cost of addition accounted for about 30% of the total treatment cost of wastewater treatment. It has only saved about 4% and has no significant economic effect.

【0003】[0003]

【発明が解決しようとする課題】上記の汚泥流出による
処理水水質の悪化防止対策として採用される、ばっ気槽
や沈殿槽に凝集剤を添加する方法は速効性はあるが、添
加を中断すると元の状態戻るので、長期安定した排水処
理を行なうことが困難であった。また、この方法は余剰
汚泥の発生量が多くなる欠点があるとともに、使用する
凝集剤の種類や添加量によっては、排水の浄化に関与す
る微生物の生育や繁殖を阻害して、処理水水質のさらな
る悪化を招く欠点があった。沈殿槽の増設やろ過装置等
の設置は、その費用において不経済であり、設置用地の
制限を受ける場合には、この方法の採用は不可能であ
る。ばっ気槽に微生物製剤を投与する方法は、その効果
が殆ど期待できず、また、シャボン液を添加して微生物
の活動を活性化して余剰汚泥発生量の減量化を図る方法
は、添加物の原料が南米等の特定地域に産する植物であ
るため、製品の価格が高く、前述のごとく総体的な排水
処理費用の低減になっていない。以上のような理由か
ら、本発明は汚泥管理面において、より容易な維持管理
で安定性が確保でき、さらに、余剰汚泥生成量が少な
く、かつ、排水処理費用の安い処理方法、すなわち、経
済上、技術上効率の高い処理方法を提供しようとするも
のである。
The method of adding a coagulant to an aeration tank or a sedimentation tank, which is adopted as a measure for preventing deterioration of the quality of treated water due to sludge outflow, is quick-acting, but when the addition is interrupted Since it returned to its original state, it was difficult to carry out stable wastewater treatment for a long period of time. In addition, this method has the drawback that the amount of excess sludge generated increases, and depending on the type and amount of coagulant used, it inhibits the growth and reproduction of microorganisms involved in the purification of wastewater, and There was a drawback that caused further deterioration. It is uneconomical in terms of cost to install an additional settling tank or install a filtering device, and this method cannot be adopted when the site for installation is restricted. The method of administering a microbial preparation to an aeration tank can hardly expect its effect, and the method of activating the activity of microorganisms by adding soap liquid to reduce the amount of excess sludge generated is Since the raw material is a plant that is produced in a specific area such as South America, the price of the product is high and the overall wastewater treatment cost has not been reduced as described above. For the above reasons, the present invention, in terms of sludge management, the stability can be secured by easier maintenance, the amount of surplus sludge generated is small, and the wastewater treatment cost is low, that is, economically. , To provide a highly efficient processing method.

【0004】[0004]

【課題を解決しようとする手段】本発明は、以上のよう
な課題を解決したもので、次のようなものである。その
特徴とするところは、排水の好気性処理工程中に天然柑
橘類から抽出した抽出物質を添加することである。この
抽出物質の原料は、ある特定地域にのみ偏在するもので
はなく、蜜柑の皮等からも抽出することができるから、
国内において容易に、かつ、安価に入手可能である。ま
た、蜜柑缶詰や蜜柑ジュース等の加工工場で処分に苦慮
している廃棄物を有効利用することができる。この抽出
物質は、イソプレンが複数個結合して天然に植物体に生
合成されたテルペンの一種である。テルペンは動植物の
ホルモン成分や光合成における重要な色素であり、香料
等としても使用されている。抽出は普通、新鮮な植物組
織をそのまま水蒸気蒸留して得られる。組織を水と混じ
て全体に水蒸気を通じて蒸留し、冷却器を通して留分を
集める。留分は一種の油であり、表面に浮上するから容
易に分離することができる。この抽出物質の排水処理に
有効な主成分はリモネンであると考えられ、オレンジの
香のする単環構造をなすモノテルペンである。この抽出
物質は水に溶解し難いので、界面活性剤等を添加して、
水に溶解し易い状態にしたものを用いることが好まし
い。本発明は、この抽出物質を排水の生物学的処理工程
中に添加することであり、抽出物質の添加は、ばっ気槽
などの好気性生物処理施設や返送汚泥、または、排水の
排出源から処理施設に至るどの箇所に行なってもよい。
抽出物質の添加量は排水の有機物成分や濃度、活性汚泥
の濃度や性状によって異なり一定ではなく、排水の特性
や系内の汚泥濃度(生物量)などに応じて決定する。こ
の抽出物質の添加が及ぼす排水処理に対する効果は、こ
の抽出物質のもつホルモン成分が、排水の浄化に関与す
る微生物に刺激を与えて活性化し、微生物の生育、増殖
を促進するためと考えられる。また、界面活性剤等を添
加して調整した本抽出物質は、さまざまな高分子物質等
の難溶解性物質を容易に溶解する性質がある。このこと
から排水中の難分解性物質の低分子化を容易にし、微生
物の代謝作用の促進に寄与しているものと考えられる。
The present invention has solved the above problems and is as follows. The feature is that the extraction substance extracted from natural citrus fruits is added during the aerobic treatment process of waste water. The raw material of this extract is not only unevenly distributed in a specific area, but can be extracted from mandarin orange peel, etc.
It is easily and cheaply available in Japan. In addition, it is possible to effectively use the waste that is difficult to dispose of at the processing plant of canned tangerine and tangerine juice. This extracted substance is a kind of terpene that is naturally biosynthesized in a plant body by combining a plurality of isoprene. Terpenes are important pigments in animal and plant hormone components and photosynthesis, and are also used as fragrances. Extraction is usually obtained by steam distillation of fresh plant tissue. The tissue is mixed with water and distilled over steam throughout and the fraction is collected through a condenser. The distillate is a kind of oil and floats on the surface so that it can be easily separated. The main component effective for the wastewater treatment of this extracted substance is considered to be limonene, which is a monoterpene having a monocyclic structure with an orange scent. Since this extracted substance is difficult to dissolve in water, add a surfactant etc.,
It is preferable to use the one that is easily dissolved in water. The present invention is to add this extract material during the biological treatment process of wastewater, the addition of the extract material from aerobic biological treatment facilities such as aeration tanks and return sludge, or the discharge source of wastewater. It can be done anywhere to the treatment facility.
The amount of the extracted substance added varies depending on the organic matter component and concentration of the wastewater, the concentration and properties of the activated sludge, and is not constant, and is determined according to the characteristics of the wastewater and the sludge concentration (biomass) in the system. It is considered that the effect of the addition of the extract substance on the wastewater treatment is that the hormone component of the extract substance stimulates and activates the microorganisms involved in the purification of the wastewater to promote the growth and proliferation of the microorganisms. In addition, the extracted substance prepared by adding a surfactant or the like has a property of easily dissolving various poorly soluble substances such as polymer substances. From this, it is considered that it facilitates the reduction of the molecular weight of the hardly decomposable substance in the waste water and contributes to the promotion of the metabolic action of microorganisms.

【0005】[0005]

【作用】本発明による排水処理方法は、従来の生物学的
処理方法における処理工程中に天然柑橘類から抽出した
抽出物質の添加工程を付与するだけであり、従来の処理
施設の変造や改造を伴うものではない。抽出物質の添加
は、人力又はポンプを使用する等機械的に行なってもよ
い。
The wastewater treatment method according to the present invention only adds the step of adding the extraction substance extracted from natural citrus to the treatment step in the conventional biological treatment method, and involves alteration or modification of the conventional treatment facility. Not a thing. The extraction substance may be added manually or mechanically such as by using a pump.

【0006】[0006]

【実施例】【Example】

実施例1 1000cc容量のメスシリンダー3本の各に、ブロイ
ラー工場の排水処理施設より採取した、活性汚泥をスキ
ムミルクを用いて順養した、初期浮遊物質濃度(MLS
S)6940mg/l、初期有機性浮遊物質濃度(ML
VSS)5480mg/lの汚泥を投入して、熱帯魚飼
育用のエアーポンプを用いてばっ気し、1日に1回、定
時にばっ気を停止し、本法と従来法との30分間静置沈
殿後の沈殿した汚泥体積比率(SV値)を測定して比較
した。SV値の測定終了後、メスシリンダー中の上澄水
を100cc引抜き、スキムミルクを水道水で溶解して
調整した、同量の人工排水(PH;5.7,BOD;3
120mg/l,COD;766mg/l,SS;79
7mg/l,総窒素;126.3mg/l,総リン;1
8.2mg/l,ノルマルヘキサン抽出物;102.9
mg/l)で満たし、再びばっ気操作を継続した。ばっ
気条件は、空気吐出量が毎分600ccのエアポンプを
用い、ばっ気時間30分間、ばっ気停止時間60分間を
交互に行なう間欠ばっ気を行なった。以上の操作におい
て、メスシリンダー中の固液分離の進行が遅く、所定容
量の上澄水の引抜きが困難なときは、静置時間を延長し
て行なった。尚、本法の実施例には人工排水の投入後、
天然柑橘類から抽出した抽出物質に界面活性剤を添加し
て調整した、表1に示す特性の原液を、蒸留水で100
00倍に希釈したものを2cc添加した。また、従来技
術による従来法1には人工排水の投入後、前記シャボン
液の原液を蒸留水で10000倍に希釈したものを2c
c添加し、従来法2には人工排水以外の物質は添加して
いない。
Example 1 Activated sludge collected from a wastewater treatment facility of a broiler factory was conditioned with skim milk in each of three graduated cylinders each having a capacity of 1000 cc.
S) 6940 mg / l, initial organic suspended solids concentration (ML
(VSS) 5480 mg / l sludge was added and aerated using an air pump for tropical fish breeding, and once a day, the aeration was stopped, and this method and conventional method were allowed to stand for 30 minutes. The sludge volume ratio (SV value) after the precipitation was measured and compared. After the measurement of the SV value was completed, 100 cc of the supernatant water in the graduated cylinder was drawn out, and skim milk was dissolved in tap water to prepare the same amount of artificial wastewater (PH; 5.7, BOD; 3).
120 mg / l, COD; 766 mg / l, SS; 79
7 mg / l, total nitrogen; 126.3 mg / l, total phosphorus; 1
8.2 mg / l, normal hexane extract; 102.9
(mg / l) and the aeration operation was continued again. As the aeration condition, an air pump having an air discharge rate of 600 cc / min was used, and intermittent aeration was performed by alternately performing an aeration time of 30 minutes and an aeration stop time of 60 minutes. In the above operation, when the solid-liquid separation in the graduated cylinder progressed slowly and it was difficult to extract a predetermined amount of the supernatant water, the standing time was extended. In addition, in the example of the present method, after the artificial drainage was added,
A stock solution having the characteristics shown in Table 1 prepared by adding a surfactant to the extracted substance extracted from natural citrus is diluted with distilled water to 100%.
2 cc was added diluted with 00 times. In addition, in the conventional method 1 according to the conventional technique, after the artificial drainage was added, the stock solution of the soap solution was diluted 10000 times with distilled water to obtain 2c.
c, and the conventional method 2 does not add any substance other than artificial drainage.

【0007】[0007]

【表1】 表2は本法、従来法1および従来法2の実施例のSV値
を示したものであり、それをグラフにしたものが図1で
ある。表2および図1から、本法、すなわち、天然柑橘
類から抽出した抽出物質を添加した方が、従来法(従来
法1および従来法2)と比較して汚泥の沈降速度が速
く、沈殿性および濃縮性の優れた活性汚泥が生成したこ
とを示している。
[Table 1] Table 2 shows SV values of Examples of the present method, the conventional method 1 and the conventional method 2, and FIG. 1 is a graph showing the SV values. From Table 2 and FIG. 1, when the present method, that is, the addition of the extraction substance extracted from natural citrus fruits, the sedimentation rate of sludge was higher than that of the conventional method (conventional method 1 and conventional method 2), and This indicates that activated sludge having excellent concentration properties was produced.

【0008】[0008]

【表2】 SV値の測定を20日間継続し、20日目の測定をで終
了した時点で、各メスシリンダーから、沈殿静置後の上
澄水を採取して水質分析用に、残余の混合液は水道水を
加えて1リットル容量にした状態の、活性汚泥浮遊物
(MLSS)および活性汚泥有機性浮遊物(MLVS
S)の測定用に供した。上澄水の水質は、本法、従来法
1および従来法2のBODは、それぞれ、6mg/l、
8mg/lおよび7mg/l、CODは、それぞれ、6
mg/l、6mg/l、8mg/lであり、本法と従来
法とではBOD、CODともに大きな差はなかった。活
性汚泥の性状については、本法、従来法1および従来法
2のMLSSは、それぞれ、7200mg/l、760
0mg/lおよび9000mg/lであり、MLVSS
は、それぞれ、5300mg/l、5700mg/lお
よび7900mg/lであった。以上から、本法のML
SSは、従来法1の約93%、従来法2の約80%であ
り、また、本法のMLVSSは従来法1の約93%、従
来法2の約67%であった。これらのことは、本法は従
来法と比較してMLSSおよびMLVSSともに減少率
が高いこと、すなわち、本発明は余剰汚泥の発生量が少
なく、沈殿性と濃縮性の優れた活性汚泥の生成する排水
処理方法を提供することを意味する。
[Table 2] The measurement of SV value was continued for 20 days, and when the measurement on the 20th day was completed by, the supernatant liquid after the precipitation was left standing was collected from each graduated cylinder, and the remaining mixed solution was tap water for water quality analysis. Activated sludge suspension (MLSS) and activated sludge organic suspension (MLVS)
It was used for the measurement of S). The BOD of the present method, the conventional method 1 and the conventional method 2 is 6 mg / l, respectively.
8 mg / l and 7 mg / l, COD is 6 respectively
It was mg / l, 6 mg / l, and 8 mg / l, and there was no significant difference in BOD and COD between this method and the conventional method. Regarding the properties of activated sludge, MLSS of this method, conventional method 1 and conventional method 2 are 7200 mg / l and 760, respectively.
0 mg / l and 9000 mg / l, MLVSS
Were 5300 mg / l, 5700 mg / l and 7900 mg / l, respectively. From the above, the ML of this method
SS was about 93% of conventional method 1 and about 80% of conventional method 2, and MLVSS of this method was about 93% of conventional method 1 and about 67% of conventional method 2. These facts indicate that the present method has a high reduction rate in both MLSS and MLVSS compared with the conventional method, that is, the present invention produces less excess sludge and produces activated sludge excellent in sedimentation and concentration. Means to provide a wastewater treatment method.

【0009】実施例2 実施例1で用いた同一試料により、処理実施開始後10
日目、15日目および20日目の本法と従来法の汚泥の
沈降状況を測定して比較した。その測定法は、ばっ気用
エアポンプを停止して180分間静置し、その間、時間
の経過と共に界面沈降する汚泥面高を記録することによ
り行なった。表3は本法、表4は従来法1、また、表5
は従来法2の処理実施開始後10日目、15日目、20
日目の経過時間と汚泥面高および経過時間と平均汚泥面
高を示しものである。また、図2は本法、従来法1およ
び従来法2の経過時間と平均汚泥界面高との関係を示す
汚泥沈降曲線である。表3、表4、表5、および図2か
ら、本法は従来法と比べて汚泥面高の減少速度が大きい
こと、すなわち、本発明は沈殿性と濃縮性の優れた活性
汚泥が生成することが判明した。
Example 2 The same sample used in Example 1 was used and 10
The sludge settling conditions of the present method and the conventional method on the days 15, 15 and 20 were measured and compared. The measurement method was performed by stopping the aeration air pump, leaving it to stand for 180 minutes, and recording the sludge surface height at which the interfacial sedimentation occurred during the time. Table 3 is this method, Table 4 is conventional method 1, and Table 5
Is the 10th, 15th, 20th day after the start of the treatment of the conventional method 2.
It shows the elapsed time on the day and the sludge height, and the elapsed time and the average sludge height. FIG. 2 is a sludge sedimentation curve showing the relationship between the elapsed time and the average sludge interface height in the present method, conventional method 1 and conventional method 2. From Table 3, Table 4, Table 5 and FIG. 2, the present method has a large reduction rate of the sludge surface height as compared with the conventional method, that is, the present invention produces activated sludge having excellent sedimentation and concentration properties. It has been found.

【0010】[0010]

【表3】 [Table 3]

【0011】[0011]

【表4】 [Table 4]

【0012】[0012]

【表5】 [Table 5]

【0013】[0013]

【発明の効果】本発明によると、沈殿性と濃縮性に富む
活性汚泥が生成するから、生物汚泥を系内に多量保持で
きるので、生物相の多様性が高くなり、食物連鎖が長く
なる。生物相が多様性に富むことは、生態系として安定
性の高さと生物化学的反応の安定性の増大を示し、水質
面においても処理効果の安定をもたらす。また、食物連
鎖が長くなると原生動物や後生動物などの食物連鎖の上
位にある生物数が多く、捕食、被食の関係が活発になる
結果、余剰汚泥の生成量が減少する。このように、本発
明によれば、沈殿性および濃縮性の優れた活性汚泥が生
成するので、沈殿槽からの汚泥流出による処理水水質の
悪化防止が容易であるため、維持管理作業の負担が軽減
でき、また、処理排水の負荷を増加する等、処理能力の
増強が可能である。本発明は、従来の処理施設に対し
て、特別な改造や変造を行なうことなく適用できるた
め、排水の排出量や水質等の過負荷により、処理能力不
足をきたしている既存施設に容易に適用可能であり、処
理経費の節減、省力、省資源、省エネルギーの面からき
わめて有効な排水処理方法である。特に、基質の有機物
が可溶性であり、さらに、それが炭水化物や低級脂肪酸
の含有量の高い、食品工場排水等の汚泥管理の困難な排
水の処理への適用効果が高い。また、本発明に係わる添
加物質の原料は天然柑橘類であるから、蜜柑の缶詰やジ
ュース加工工場等から排出される廃棄物の有効利用に貢
献できる。
EFFECTS OF THE INVENTION According to the present invention, activated sludge rich in sedimentation and concentration is produced, so that a large amount of biological sludge can be retained in the system, the diversity of biota becomes high, and the food chain becomes long. The rich diversity of biota shows high stability as an ecosystem and increased stability of biochemical reactions, and stabilizes the treatment effect in terms of water quality. In addition, as the food chain becomes longer, the number of organisms higher in the food chain, such as protozoa and metazoans, increases, and as a result of active predation and prey, the amount of excess sludge produced decreases. As described above, according to the present invention, since activated sludge having excellent sedimentation and concentration properties is generated, it is easy to prevent deterioration of treated water quality due to sludge outflow from the sedimentation tank, thus burdening maintenance work. It is possible to reduce the amount of wastewater and increase the treatment capacity by increasing the load of treated wastewater. INDUSTRIAL APPLICABILITY Since the present invention can be applied to a conventional treatment facility without any special modification or alteration, it can be easily applied to an existing facility that has a shortage of treatment capacity due to an overload of wastewater discharge amount or water quality. It is possible and is a very effective wastewater treatment method from the viewpoint of saving treatment cost, labor saving, resource saving and energy saving. In particular, the organic substance of the substrate is soluble, and further, it has a high application effect to the treatment of wastewater having a high content of carbohydrates and lower fatty acids, which is difficult to manage sludge such as wastewater from food factories. Further, since the raw material of the additive substance according to the present invention is natural citrus fruits, it can contribute to the effective use of wastes discharged from canned tangerines and juice processing plants.

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

【図1】実施例1のSV値。FIG. 1 is an SV value of Example 1.

【図2】実施例2の汚泥沈降曲線。FIG. 2 is a sludge settling curve of Example 2.

【符号の説明】[Explanation of symbols]

1 本発明のSV値 2 従来法1のSV値 3 従来法2のSV値 4 本発明の汚泥沈降曲線 5 従来法1の汚泥沈降曲線 6 従来法2の汚泥沈降曲線 1 SV Value of the Present Invention 2 SV Value of Conventional Method 1 SV Value of Conventional Method 2 4 Sludge Settling Curve of the Present Invention 5 Sludge Settling Curve of Conventional Method 1 6 Sludge Settling Curve of Conventional Method 2

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 排水を生物学的に処理する工程中に、天
然柑橘類から抽出した抽出物質を添加することを特徴と
する排水処理方法。
1. A method for treating wastewater, which comprises adding an extraction substance extracted from natural citrus during the step of biologically treating the wastewater.
【請求項2】 生物学的処理工程は、好気性微生物を利
用して行なうものである請求項1記載の排水処理方法。
2. The wastewater treatment method according to claim 1, wherein the biological treatment step is performed by utilizing aerobic microorganisms.
【請求項3】 抽出物質の添加は、排水の排出源から排
水処理施設に至る途中において行なうものである請求項
1又は2記載の排水処理方法。
3. The wastewater treatment method according to claim 1, wherein the extraction substance is added on the way from the drainage source to the wastewater treatment facility.
【請求項4】 抽出物質の添加は、ばっ気槽において行
なうものである請求項1又は2記載の排水処理方法。
4. The wastewater treatment method according to claim 1, wherein the extraction substance is added in an aeration tank.
【請求項5】 抽出物質の添加は、返送汚泥中に行なう
ものである請求項1又は2記載の排水処理方法。
5. The wastewater treatment method according to claim 1, wherein the extraction substance is added to the returned sludge.
JP5179735A 1993-06-11 1993-06-11 Waste water treatment Pending JPH07982A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5179735A JPH07982A (en) 1993-06-11 1993-06-11 Waste water treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5179735A JPH07982A (en) 1993-06-11 1993-06-11 Waste water treatment

Publications (1)

Publication Number Publication Date
JPH07982A true JPH07982A (en) 1995-01-06

Family

ID=16070958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5179735A Pending JPH07982A (en) 1993-06-11 1993-06-11 Waste water treatment

Country Status (1)

Country Link
JP (1) JPH07982A (en)

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