JP2000210074A - Acclimation of degrading microorganism, obtaining of acclimated microorganism and degradation of organic compound - Google Patents
Acclimation of degrading microorganism, obtaining of acclimated microorganism and degradation of organic compoundInfo
- Publication number
- JP2000210074A JP2000210074A JP11013037A JP1303799A JP2000210074A JP 2000210074 A JP2000210074 A JP 2000210074A JP 11013037 A JP11013037 A JP 11013037A JP 1303799 A JP1303799 A JP 1303799A JP 2000210074 A JP2000210074 A JP 2000210074A
- Authority
- JP
- Japan
- Prior art keywords
- organic compound
- degrading
- degrading microorganism
- microorganism
- liquid
- 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
Links
- 150000002894 organic compounds Chemical class 0.000 title claims abstract description 37
- 230000000593 degrading effect Effects 0.000 title claims abstract description 27
- 244000005700 microbiome Species 0.000 title abstract description 23
- 230000015556 catabolic process Effects 0.000 title abstract 4
- 238000006731 degradation reaction Methods 0.000 title abstract 4
- 238000000034 method Methods 0.000 claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 241000894006 Bacteria Species 0.000 claims description 31
- 150000002898 organic sulfur compounds Chemical class 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000003002 pH adjusting agent Substances 0.000 claims description 6
- 238000006065 biodegradation reaction Methods 0.000 abstract description 7
- 239000001963 growth medium Substances 0.000 abstract description 4
- 238000012258 culturing Methods 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 238000001556 precipitation Methods 0.000 abstract 1
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 239000010802 sludge Substances 0.000 description 13
- 150000001875 compounds Chemical class 0.000 description 9
- 238000004062 sedimentation Methods 0.000 description 8
- 239000002351 wastewater Substances 0.000 description 8
- 238000005273 aeration Methods 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 5
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000007513 acids Chemical group 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 239000002609 medium Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical class [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- -1 dimethyl sulfone Chemical compound 0.000 description 2
- 230000005764 inhibitory process Effects 0.000 description 2
- 229910052751 metal Chemical class 0.000 description 2
- 239000002184 metal Chemical class 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 description 2
- HHVIBTZHLRERCL-UHFFFAOYSA-N sulfonyldimethane Chemical compound CS(C)(=O)=O HHVIBTZHLRERCL-UHFFFAOYSA-N 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 206010052804 Drug tolerance Diseases 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 230000003139 buffering effect Effects 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
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012776 electronic material Substances 0.000 description 1
- 210000000416 exudates and transudate Anatomy 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 230000026781 habituation Effects 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000002054 inoculum Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 125000004434 sulfur atom Chemical group 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
Landscapes
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は有機化合物分解菌の
馴養または馴養菌の取得方法、および有機化合物の分解
方法に関するものである。[0001] The present invention relates to a method for acclimating or decomposing organic compound-decomposing bacteria, and a method for decomposing organic compounds.
【0002】[0002]
【従来の技術】廃水に含まれる有機化合物の生物学的処
理法はいくつかあるが、その中で最も汎用的な方法とし
ては活性汚泥法が挙げられる。本法は好気的処理法であ
り、被処理水としての原水を貯留する貯留槽と、該貯留
槽から供給される被処理水のpHを調整するためのpH
調整槽と、そのpH調整槽によってpHが調整された被
処理水を生物処理するための生物処理槽と、その生物処
理槽で処理された被処理水を供給する沈殿槽から構成さ
れている。上記pH調整槽内には、そのpH調整槽内の
pHを測定するpH測定計と、pH調整液を前記pH調
整槽内に供給するポンプと、前記pH測定計で測定され
たpHに応じて前記ポンプによるpH調整液供給量を制
御する制御装置とが設けられている。このような処理装
置においては、被処理水は貯留槽にて一時的に貯留され
た後、pH調整槽にて所定のpH値となるまでpH調整
液が添加され、その後生物処理槽へ供給される。被処理
水は生物処理槽内で、活性汚泥中に存在する好気性微生
物による酸化分解を受けるが、これに必要な酸素は生物
処理槽内に配設された曝気装置によって順次供給され
る。生物処理槽で処理された被処理水は、その後沈殿槽
にて微生物を含む汚泥と処理水を分離し、沈殿分離され
た汚泥は生物処理槽に返送するか、又は系外に引き抜か
れる。活性汚泥中の好気性微生物は多種存在し、その構
成は被処理水中の有機化合物の構成によって異なる。こ
れは長期にわたり馴養することによって、該被処理水に
最適な微生物の構成となる。この結果活性汚泥は、種々
雑多な有機化合物を一度に処理できると言う最大の特徴
を有することになるが、反面単位体積あたりの処理能力
が低い、急激な被処理水の変化に対応できない、酸素供
給動力費が嵩む、等の欠点がある。特に高負荷化合物が
混入することによってその欠点が著しく増幅される場合
がある。このような化合物の例としては硫黄原子を分子
中に有するジメチルスルホキシド(以下DMSO)が挙
げられる。DMSOは難分解性で、酸素供給が低下する
と還元されてジメチルスルフィド等の悪臭物質を生成す
るため、確実に処理するには、滞留時間を増やし、酸素
供給量を増強する必要があり、活性汚泥法で他の化合物
と同時に処理すると、処理費が更に嵩むことになる。ま
たDMSO等では基質濃度があるレベル以上になると生
物に対する阻害が生じるため、他の有機化合物の分解速
度まで低下を引き起こす原因に成りかねない。またDM
SOは分解されると通常は硫酸を生じるため著しくpH
が低下するが、生物処理槽が大規模になればなるほどp
Hを適切に維持しながらアルカリ液を供給してpHを安
定に維持することが困難となってくる。一方DMSOは
半導体等電子材料の洗浄という特殊用途に用いられるこ
とから分別が容易である。従って高負荷の化合物を含み
他の廃水から分別可能な廃水については、個別に処理す
るほうが効率的な場合がある。これまでにもDMSOに
関する個別対応の処理法や処理システムがいくつか提案
されている。例を挙げると、有機硫黄化合物を含有する
被処理水のpHを調整した後生物処理槽で処理する方法
(特開平7−265890号公報)、酸化処理した後生
物的化学処理する方法(特開平8−238497号公
報)、DMSOにて馴養した微生物を包括固定したPV
Aを主体としたゲルを用いた処理方法(特開平7−31
991号公報)などである。2. Description of the Related Art There are several biological treatment methods for organic compounds contained in wastewater, and the most versatile method is the activated sludge method. This method is an aerobic treatment method, and includes a storage tank for storing raw water as the water to be treated, and a pH for adjusting the pH of the water to be treated supplied from the storage tank.
It is composed of an adjusting tank, a biological treatment tank for biologically treating the water to be treated, the pH of which is adjusted by the pH adjusting tank, and a sedimentation tank for supplying the treated water treated in the biological treatment tank. In the pH adjusting tank, a pH meter for measuring the pH in the pH adjusting tank, a pump for supplying a pH adjusting solution into the pH adjusting tank, and a pH measured by the pH meter are used. And a control device for controlling the supply amount of the pH adjusting liquid by the pump. In such a treatment apparatus, after the water to be treated is temporarily stored in a storage tank, a pH adjusting solution is added in the pH adjusting tank until the water reaches a predetermined pH value, and then supplied to the biological treatment tank. You. The water to be treated undergoes oxidative degradation by aerobic microorganisms present in the activated sludge in the biological treatment tank, and the oxygen required for this is sequentially supplied by an aeration device disposed in the biological treatment tank. The to-be-processed water treated in the biological treatment tank is then separated into sludge containing microorganisms and treated water in a sedimentation tank, and the sludge separated and separated is returned to the biological treatment tank or pulled out of the system. There are many types of aerobic microorganisms in activated sludge, and their composition differs depending on the composition of organic compounds in the water to be treated. This becomes the most suitable microbial composition for the water to be treated after long-term acclimation. As a result, activated sludge has the greatest feature of being able to treat various organic compounds at once, but on the other hand, has low treatment capacity per unit volume, cannot cope with rapid changes in the water to be treated, and has a high oxygen content. There are drawbacks such as increased supply power cost. In particular, the incorporation of a highly loaded compound may significantly amplify the disadvantage. Examples of such a compound include dimethyl sulfoxide having a sulfur atom in the molecule (hereinafter, DMSO). DMSO is difficult to decompose, and when oxygen supply is reduced, it is reduced to generate malodorous substances such as dimethyl sulfide. Therefore, in order to surely treat DMSO, it is necessary to increase the residence time and increase the oxygen supply amount, If the compound is treated simultaneously with other compounds by the method, the treatment cost will be further increased. In addition, in the case of DMSO or the like, if the substrate concentration exceeds a certain level, an inhibition of the organism occurs, which may cause a decrease in the decomposition rate of other organic compounds. Also DM
When SO is decomposed, it usually produces sulfuric acid.
Decreases, but the larger the biological treatment tank, the larger the p
It becomes difficult to supply the alkaline solution and maintain the pH stably while appropriately maintaining H. On the other hand, DMSO is easy to separate because it is used for special purposes such as cleaning of electronic materials such as semiconductors. Therefore, it may be more efficient to treat wastewater containing a compound having a high load and being separable from other wastewater individually. Some individual processing methods and processing systems for DMSO have been proposed so far. For example, a method of adjusting the pH of water to be treated containing an organic sulfur compound and then treating the treated water in a biological treatment tank (Japanese Patent Application Laid-Open No. 7-265890), a method of oxidizing and then performing a biological chemical treatment (Japanese Patent Application Laid-Open No. JP-A-8-238497), PV in which microorganisms acclimated in DMSO are comprehensively fixed.
A processing method using a gel mainly composed of A (JP-A-7-31)
No. 991).
【0003】[0003]
【発明が解決しようとする課題】しかしながら、個別処
理を行う場合、当然活性汚泥法に比べてその化合物の濃
度が高くなり、通常の分解微生物では生育阻害を引き起
こすなどの問題が生じる。これらの欠点を克服してはじ
めて処理の効率化が得られることになる。すなわち、そ
の化合物を効率よく分解処理するためには、その分解条
件に最も適した、能力の高い微生物を、いかに効率よく
短時間で馴養、取得するかが最大の鍵となるが、その方
法に関しては経験や勘に頼っているのが現状である。However, in the case of individual treatment, the concentration of the compound is naturally higher than in the activated sludge method, which causes problems such as the inhibition of the growth of ordinary degrading microorganisms. Only when these disadvantages are overcome, efficiency of the processing can be obtained. In other words, in order to efficiently decompose the compound, the most important factor is how to acclimate and acquire a microorganism having the highest ability that is most suitable for the decomposition conditions in a short time. Is currently relying on experience and intuition.
【0004】[0004]
【課題を解決するための手段】すなわち、本発明は以下
の構成からなる。That is, the present invention comprises the following constitutions.
【0005】「有機化合物分解性の分解菌を液中で馴養
する方法であって、分解菌が有機化合物を生分解するこ
とによって系のpHを変動させるものであり、馴養中に
pHの変動に伴い一定のpH範囲内となるようにpH調
整剤および分解対象有機化合物を液中に添加することを
特徴とする分解菌の馴養方法。」、「馴養液中のpH範
囲が6〜8であることを特徴とする前記、分解菌の分解
菌馴養方法。」、「馴養液のpH調整剤にアルカリ剤が
含まれていることを特徴とする前回いずれかの分解菌の
馴養方法。」、「分解菌の分解対象有機化合物に有機硫
黄化合物が含まれていることを特徴とする前記いずれか
の分解菌の馴養方法。」、「前記いずれかの分解菌の馴
養の後、得られた菌を取り出すことを特徴とする馴養菌
の取得方法。」、「前記いずれかに記載の方法で分解菌
を馴養後、分解菌を含有する液に分解対象有機化合物を
添加することを特徴とする有機化合物の分解方法。」、
「分解対象有機化合物が有機硫黄化合物である前記有機
化合物の分解方法。」[0005] This is a method of acclimating an organic compound-degrading decomposing bacterium in a liquid, wherein the degrading bacterium biodegrades the organic compound to change the pH of the system. A method for acclimating degrading bacteria, characterized by adding a pH adjuster and an organic compound to be decomposed to a liquid so as to be within a certain pH range. "," The pH range in the acclimated liquid is 6-8. " The method of acclimating degrading bacteria of the degrading bacteria, the method of acclimating any one of the preceding degrading bacteria, wherein the pH adjusting agent of the solution contains an alkali agent. The method for acclimating any of the degrading bacteria, wherein the organic compound to be decomposed by the degrading bacteria contains an organic sulfur compound. " A method for obtaining an acclimatized bacterium, which is characterized by being taken out. ", Method for decomposing organic compounds characterized by the addition of decomposed organic compound decomposing bacteria by the method described in the one after acclimatization, to a solution containing the decomposing bacteria. "
"A method for decomposing the organic compound, wherein the organic compound to be decomposed is an organic sulfur compound."
【0006】[0006]
【発明の実施の形態】以下に本発明を詳細に説明する。
本発明の方法が有効に作用する排水中の分解対象有機化
合物は、生分解によってpHが一方に著しく変動するも
のが好ましく使用される。生分解によってpHが低下す
る例としては、DMSOの他にジメチルスルホンなどの
有機硫黄化合物、1〜3級アミン、4級アンモニウム塩
などの窒素化合物などがあり、pHが上昇する例として
は、各種有機酸塩が挙げられる。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail.
As the organic compound to be decomposed in the wastewater on which the method of the present invention effectively acts, those whose pH significantly fluctuates to one side due to biodegradation are preferably used. Examples of the decrease in pH due to biodegradation include, in addition to DMSO, organic sulfur compounds such as dimethyl sulfone, and nitrogen compounds such as primary to tertiary amines and quaternary ammonium salts. Organic acid salts are mentioned.
【0007】pH調整剤は、分解対象有機化合物自身が
調整剤としての緩衝作用を持つ場合、例えば生分解によ
ってpHが低下する場合にアルカリ性化合物である場
合、または生分解によってpHが上昇する場合に酸性化
合物である場合には特に添加する必要はないが、そのよ
うな作用を持たない、即ち中性の場合は、生分解によっ
てpHが低下する場合は各種アルカリ剤、上昇する場合
は酸類を用いる。何れも有機、無機どちらでも使用可能
であるが、新たな分解への負荷を加えることが好ましく
ない場合は、無機剤を用いるのが無難である。無機アル
カリ剤としては水酸化ナトリウム、水酸化カリウム、水
酸化カルシウム、炭酸ナトリウム、炭酸カリウム、炭酸
水素ナトリウムなどがあるが、鉄その他の金属塩を含有
する排水の場合強アルカリでは沈殿するので、そのこと
が微生物の生育に影響するような場合は炭酸水素ナトリ
ウムのような弱酸を添加するのが好ましい。酸類では一
般に硫酸、塩酸等の無機酸が用いられる。その添加量は
生分解によって変動する際に生成する変動物質、すなわ
ち酸あるいはアルカリ、の量より若干少ない量であるこ
とが重要である。同量あるいはそれ以上の場合、処理槽
内の化合物が完全に分解処理され、もはやpHの変動が
起こらなくなるからである。The pH adjuster is used when the organic compound to be decomposed itself has a buffering action as an adjuster, for example, when the pH is lowered by biodegradation, or when it is an alkaline compound, or when the pH is increased by biodegradation. When it is an acidic compound, it is not particularly necessary to add it, but it does not have such an effect, that is, when it is neutral, various alkaline agents are used when the pH is reduced by biodegradation, and when it is increased, acids are used. . Either organic or inorganic can be used, but when it is not preferable to add a new load to decomposition, it is safe to use an inorganic agent. Inorganic alkali agents include sodium hydroxide, potassium hydroxide, calcium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogen carbonate, etc.In the case of wastewater containing iron and other metal salts, strong alkali precipitates, If this affects the growth of the microorganism, it is preferable to add a weak acid such as sodium bicarbonate. In general, inorganic acids such as sulfuric acid and hydrochloric acid are used as the acids. It is important that the amount of addition is slightly smaller than the amount of a variable substance generated when the substance fluctuates by biodegradation, that is, an acid or an alkali. If the amount is the same or more, the compound in the treatment tank is completely decomposed and the pH no longer fluctuates.
【0008】その他の添加物としては、各種窒素源、リ
ン源、イオウ源、微量無機金属塩など微生物の生育に必
要な物質が分解対象有機化合物に含まれない場合は、必
要に応じて添加することが好ましい。[0008] As other additives, if substances necessary for the growth of microorganisms such as various nitrogen sources, phosphorus sources, sulfur sources and trace inorganic metal salts are not included in the organic compounds to be decomposed, they are added as necessary. Is preferred.
【0009】馴養時の条件は個々の分解対象有機化合物
の排水中の状況により、自由に選択されるが、、DMS
Oのような有機硫黄化合物について述べれば、調節すべ
きpHはpH4〜10が好ましく、pH6〜8がより好
ましい。馴養時の分解対象有機化合物の濃度は100p
pm以上10%以下(ppmおよび%は特に断りのない
限り重量基準を意味する)が好ましく、300ppm以
上1%以下がより好ましい。水温は10〜40℃が好ま
しく、25〜35℃がより好ましい。DMSOの分解菌
は通常好気性微生物であるため酸素の供給が必要である
が、その際水中の溶存酸素濃度は1ppm以上が好まし
く、2ppm以上がより好ましい。また、曝気のみでも
自然に分解菌が発生してくるが、馴養開始時に土壌滲出
液や汚泥などの種菌を入れることによって分解菌の馴養
期間を短縮することができる。The conditions at the time of acclimation can be freely selected according to the situation in the wastewater of each organic compound to be decomposed.
With respect to organic sulfur compounds such as O, the pH to be adjusted is preferably pH 4-10, more preferably pH 6-8. The concentration of organic compounds to be decomposed at the time of habituation is 100p
It is preferably from pm to 10% (ppm and% mean weight basis unless otherwise specified), and more preferably from 300 ppm to 1%. The water temperature is preferably from 10 to 40C, more preferably from 25 to 35C. Since DMSO-degrading bacteria are usually aerobic microorganisms, it is necessary to supply oxygen. At this time, the dissolved oxygen concentration in water is preferably 1 ppm or more, more preferably 2 ppm or more. Decomposing bacteria are naturally generated only by aeration, but the acclimatization period of the decomposing bacteria can be shortened by adding seeds such as soil exudate and sludge at the start of acclimation.
【0010】分解菌の馴養に用いる装置としては、処理
槽内の廃水滞留領域に常時曝気させる曝気機構、pHを
調整するためのpHセンサーとコントローラーおよびp
H調整剤を含有した分解対象有機化合物を供給するため
のポンプを備えているものが使用できる。更に沈殿槽を
備えることにより、沈降性のある微生物あるいは微生物
凝集物を処理槽内に濃縮せしめることが出来る。沈殿槽
の体積が小さいほど濃縮される微生物の沈降性は良好と
なる。また小さければ処理槽内に組み込むことも可能で
ある。また沈降性良好であればより少ない滞留時間でも
処理が可能であり、従って低濃度の分解対象有機化合物
でも単位容積当りの処理量を損なうことなく処理するこ
とが可能となる。[0010] As an apparatus used for acclimatization of the decomposing bacteria, an aeration mechanism for constantly aerating the wastewater retention region in the treatment tank, a pH sensor and a controller for adjusting pH, and a p-type device.
A device equipped with a pump for supplying an organic compound to be decomposed containing an H adjustor can be used. Further, by providing a sedimentation tank, sedimentable microorganisms or microbial aggregates can be concentrated in the treatment tank. The smaller the volume of the sedimentation tank, the better the sedimentation property of the concentrated microorganisms. Moreover, if it is small, it can be incorporated in the processing tank. If the sedimentation is good, the treatment can be carried out even with a shorter residence time, so that even a low-concentration organic compound to be decomposed can be treated without impairing the treatment amount per unit volume.
【0011】本発明の方法で馴養した後、分解菌を含有
する液に分解対象有機化合物を添加すれば有機化合物の
分解が可能となる。After acclimation by the method of the present invention, the organic compound can be decomposed by adding an organic compound to be decomposed to the solution containing the decomposing bacteria.
【0012】[0012]
【実施例】以下に本発明の実施例を説明する。Embodiments of the present invention will be described below.
【0013】図1において、生物処理槽1はpH調整剤
と分解対象有機化合物である培地4を生物処理するため
のもので、この生物処理槽1内の排水滞留領域には常時
曝気させる曝気機構2と、曝気個所の上方に配して排水
滞留領域に設けられた筒状の循還流形成体3を備えてお
り、流量は流量計(図示していない)によって制御され
ている。さらに生物処理槽1内にはpHを測定するpH
センサー6と、pH変動に伴い培地4を生物処理槽1内
に供給する供給手段であるpHコントローラー7が具備
されている。また生物処理槽から流出した分解菌を捕捉
するための沈殿槽5を生物処理槽1内に持っている。In FIG. 1, a biological treatment tank 1 is for biological treatment of a pH adjusting agent and a culture medium 4 which is an organic compound to be decomposed, and an aeration mechanism for constantly aerating a drainage retention region in the biological treatment tank 1. 2 and a cylindrical circulation forming body 3 provided above the aeration point in the drainage retention area, and the flow rate is controlled by a flow meter (not shown). Further, a pH for measuring pH is set in the biological treatment tank 1.
A sensor 6 and a pH controller 7 serving as a supply unit for supplying the culture medium 4 into the biological treatment tank 1 in accordance with a change in pH are provided. Further, a sedimentation tank 5 for capturing the decomposing bacteria flowing out of the biological treatment tank is provided in the biological treatment tank 1.
【0014】[実施例1]図1に示す形態の処理装置を準
備し、ジメチルスルホキシド 0.2%、NaHCO
3 0.36%、NH4Cl 0.04%、K2HPO4
0.02%、MgCl2 0.02%からなる培地4を
調製し処理槽1に投入した。これに種菌として、DMS
O含有排水を処理している工場内活性汚泥装置の汚泥を
添加し、25℃で培養を開始した。調整pHを7とし
て、pH低下に伴って培地4からpHコントローラー7
を通じて培地の一部が供給されるようにした。また処理
槽内のDMSO濃度はガスクロマトグラフィーによって
測定した。3日後処理槽容量(L)に対する1日の処理
量が0.14Lで、処理液のDMSO濃度が1000p
pm(0.04g−DMSO/L/日)であったのが、
30日後処理槽内の汚泥の沈降性が良好となり処理量が
1.8Lで、処理液のDMSO濃度が450ppm(7
g−DMSO/L/日)となった。この時、汚泥の乾燥
重量(MLSS)は20g/Lであった。Example 1 A processing apparatus having the form shown in FIG. 1 was prepared, and dimethyl sulfoxide 0.2% and NaHCO 3 were prepared.
3 0.36%, NH 4 Cl 0.04%, K 2 HPO 4
A medium 4 composed of 0.02% and 0.02% of MgCl 2 was prepared and charged into the treatment tank 1. DMS as the inoculum
The sludge of the activated sludge device in the factory that is treating the O-containing wastewater was added, and the culture was started at 25 ° C. The pH was adjusted to 7 and the pH controller 7
A part of the culture medium was supplied through. The DMSO concentration in the treatment tank was measured by gas chromatography. After 3 days, the processing volume per day with respect to the processing tank capacity (L) is 0.14 L, and the DMSO concentration of the processing solution is 1000 p.
pm (0.04 g-DMSO / L / day)
After 30 days, the sedimentation of the sludge in the treatment tank became good, the treatment amount was 1.8 L, and the DMSO concentration of the treatment liquid was 450 ppm (7 ppm).
g-DMSO / L / day). At this time, the dry weight (MLSS) of the sludge was 20 g / L.
【0015】[実施例2]実施例1の馴養状態(7g−
DMSO/L/日)で、調整するpHを6〜8に変えて
処理を行った結果、pH6.5〜7.5で処理量が最大
であり、pH6.0ではその20%、pH8ではその4
5%であった。Example 2 Condition of acclimation in Example 1 (7 g
(DMSO / L / day), the treatment was carried out by changing the pH to be adjusted to 6 to 8. As a result, the treatment amount was maximum at pH 6.5 to 7.5, 20% at pH 6.0, and 20% at pH 8. 4
5%.
【0016】[実施例3]実施例1の馴養状態(7g−
DMSO/L/日)で、調整するpHを7とし、供給す
る培地濃度を2000〜500ppmに希釈して処理を
行った結果、2000〜1000ppmでは処理量を損
なうことなく処理でき、500ppmではその80%で
あった。また、このときの汚泥の乾燥重量は20〜26
g/Lであった。[Embodiment 3] The acclimatized state of Embodiment 1 (7 g-
(DMSO / L / day), the pH to be adjusted was set to 7, and the concentration of the medium to be supplied was diluted to 2000 to 500 ppm. As a result, the treatment could be carried out at 2000 to 1000 ppm without impairing the treatment amount. %Met. The dry weight of the sludge at this time is 20 to 26.
g / L.
【0017】[0017]
【発明の効果】本発明においては、生物処理槽内のpH
変動に伴い一定のpH範囲内となるように連続的にpH
調整剤および分解対象有機化合物が供給されるため、そ
の時点の馴養状態で処理可能な限界量を常に自動的に供
給することができる。このため、分解菌の馴養を最短時
間で実施することができ、ひいては馴養菌の取得が容易
に可能となる。また本方式で処理すれば常に最大限の処
理量が維持されるため、装置のコンパクト化が可能とな
る。According to the present invention, the pH in the biological treatment tank is adjusted.
The pH is continuously adjusted to be within a certain pH range with fluctuation.
Since the adjusting agent and the organic compound to be decomposed are supplied, the limit amount that can be processed in the acclimatized state at that time can always be supplied automatically. Therefore, the acclimatization of the decomposed bacteria can be performed in the shortest time, and thus, the acclimatized bacteria can be easily obtained. In addition, if the processing is performed by this method, the maximum processing amount is always maintained, so that the apparatus can be downsized.
【図1】本発明に係わるDMSOの処理装置の一実施例
を示す概念図である。FIG. 1 is a conceptual diagram showing an embodiment of a DMSO processing apparatus according to the present invention.
1・・・生物処理槽、2・・・曝気機構、3・・・循還流形成
体、4・・・培地、5・・・沈殿槽、6・・・pHセンサー、7・
・・pHコントローラーDESCRIPTION OF SYMBOLS 1 ... Biological treatment tank, 2 ... Aeration mechanism, 3 ... Circulating body, 4 ... Medium, 5 ... Settling tank, 6 ... pH sensor, 7
..PH controller
Claims (7)
る方法であって、分解菌が有機化合物を生分解すること
によって系のpHを変動させるものであり、馴養中にp
Hの変動に伴い一定のpH範囲内となるようにpH調整
剤および分解対象有機化合物を液中に添加することを特
徴とする分解菌の馴養方法。1. A method of acclimating an organic compound-degrading decomposing bacterium in a liquid, wherein the degrading bacterium biodegrades an organic compound to change the pH of the system.
A method for acclimating a decomposing bacterium, comprising adding a pH adjuster and an organic compound to be decomposed to a liquid so as to fall within a certain pH range with the fluctuation of H.
特徴とする請求項1記載の分解菌の分解菌馴養方法。2. The method according to claim 1, wherein the pH of the solution is in the range of 6 to 8.
ていることを特徴とする請求項1または2記載の分解菌
の馴養方法。3. The method for acclimating degrading bacteria according to claim 1, wherein an alkaline agent is contained in the pH adjuster of the acclimating liquid.
合物が含まれていることを特徴とする請求項1〜3に記
載の分解菌の馴養方法。4. The method for acclimating a degrading bacterium according to claim 1, wherein the organic compound to be decomposed by the degrading bacterium contains an organic sulfur compound.
後、得られた菌を取り出すことを特徴とする馴養菌の取
得方法。5. A method for obtaining a cultivated bacterium, which comprises removing the bacterium obtained after acclimation of the degrading bacterium according to any one of claims 1 to 4.
解菌を馴養後、分解菌を含有する液に分解対象有機化合
物を添加することを特徴とする有機化合物の分解方法。6. A method for decomposing an organic compound, comprising acclimating a degrading bacterium by the method according to any one of claims 1 to 4, and then adding an organic compound to be decomposed to a liquid containing the degrading bacterium.
る請求項6記載の有機化合物の分解方法。7. The method for decomposing an organic compound according to claim 6, wherein the organic compound to be decomposed is an organic sulfur compound.
Priority Applications (1)
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JP11013037A JP2000210074A (en) | 1999-01-21 | 1999-01-21 | Acclimation of degrading microorganism, obtaining of acclimated microorganism and degradation of organic compound |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006500711A (en) * | 2002-09-25 | 2006-01-05 | インフィネオン テヒノロギーズ アーゲー | Update control circuit for IC having memory array |
JP2006142192A (en) * | 2004-11-18 | 2006-06-08 | Kurita Water Ind Ltd | Wastewater treatment equipment containing organic sulfur compounds |
JP2012251937A (en) * | 2011-06-06 | 2012-12-20 | Hitachi High-Technologies Corp | Preprocessor and automatic analyzer using the same |
CN106745795A (en) * | 2016-08-01 | 2017-05-31 | 宜态科水务技术(上海)有限公司 | A kind of full-automatic wastewater processes bio-synergistic device |
-
1999
- 1999-01-21 JP JP11013037A patent/JP2000210074A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006500711A (en) * | 2002-09-25 | 2006-01-05 | インフィネオン テヒノロギーズ アーゲー | Update control circuit for IC having memory array |
JP2006142192A (en) * | 2004-11-18 | 2006-06-08 | Kurita Water Ind Ltd | Wastewater treatment equipment containing organic sulfur compounds |
JP4670322B2 (en) * | 2004-11-18 | 2011-04-13 | 栗田工業株式会社 | Wastewater treatment equipment containing organic sulfur compounds |
JP2012251937A (en) * | 2011-06-06 | 2012-12-20 | Hitachi High-Technologies Corp | Preprocessor and automatic analyzer using the same |
CN106745795A (en) * | 2016-08-01 | 2017-05-31 | 宜态科水务技术(上海)有限公司 | A kind of full-automatic wastewater processes bio-synergistic device |
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