JP2007021313A - Volume reduction method of sludge, method for causing bacteria group mainly comprising bacillus to dominate, and organic wastewater treatment method using the dominating method - Google Patents
Volume reduction method of sludge, method for causing bacteria group mainly comprising bacillus to dominate, and organic wastewater treatment method using the dominating method Download PDFInfo
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- 239000010802 sludge Substances 0.000 title claims abstract description 89
- 241000193830 Bacillus <bacterium> Species 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 42
- 241000894006 Bacteria Species 0.000 title claims abstract description 16
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 15
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 title abstract 3
- 239000012530 fluid Substances 0.000 claims abstract description 49
- 244000005700 microbiome Species 0.000 claims abstract description 30
- 230000003381 solubilizing effect Effects 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000002904 solvent Substances 0.000 claims description 17
- 239000002351 wastewater Substances 0.000 claims description 13
- 239000010815 organic waste Substances 0.000 claims description 9
- 230000001580 bacterial effect Effects 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 6
- 238000012258 culturing Methods 0.000 claims description 3
- 235000015097 nutrients Nutrition 0.000 claims description 3
- 238000003672 processing method Methods 0.000 claims description 3
- 238000005273 aeration Methods 0.000 claims description 2
- 208000024891 symptom Diseases 0.000 claims 1
- 238000005063 solubilization Methods 0.000 description 9
- 230000007928 solubilization Effects 0.000 description 9
- 235000019645 odor Nutrition 0.000 description 5
- 210000000170 cell membrane Anatomy 0.000 description 3
- 210000002421 cell wall Anatomy 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000010979 pH adjustment Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Activated Sludge Processes (AREA)
- Physical Water Treatments (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
本発明は、汚泥可溶化装置を用いた、微生物の可溶化方法、バチルス属を主体とする細菌群の優占化方法、及び該優占化方法を用いた有機性排水の処理方法に関し、特に同一の汚泥可溶化装置で2回以上処理すること、および最初の処理時には空気を供給せず、最後の処理時に空気を供給することを特徴とする、微生物の可溶化方法、バチルス属を主体とする細菌群の優占化方法、及び該優占化方法を用いた有機性排水の処理方法に関する。 The present invention relates to a method for solubilizing microorganisms using a sludge solubilizer, a method for predominating bacteria belonging to the genus Bacillus, and a method for treating organic wastewater using the method for predominance, A method for solubilizing microorganisms, mainly consisting of the genus Bacillus, characterized in that the treatment is performed twice or more in the same sludge solubilizer, and air is not supplied at the first treatment but air is supplied at the last treatment. The present invention relates to a method for predominating bacterial groups, and a method for treating organic wastewater using the predominance method.
活性汚泥法に代表されるように、従来、微生物を利用する排水処理方法が広く普及している。この場合、排水処理に伴って大量に発生する余剰汚泥をいかに処理するかは大きな問題である。汚泥を脱水して焼却する方法はコストが高く、汚泥の一部を処理槽に返送する方法にも限界がある。そこで、汚泥を可溶化してから返送することもなされ、そのための汚泥可溶化装置として機能する気液混合装置も開発されている(例えば、特許文献1〜2)。
一方、近年、バチルス菌を用いて排水処理を行うことにより、処理水質の向上、余剰汚泥の発生量の削減、及び悪臭の抑制を図ることが提案されている(特許文献3〜5)。しかしながら、バチルス菌を大容量の生物処理槽へ添加すると、菌濃度が低下するために菌の活力も低下し、バチルス菌本来の性能を発揮することが困難である。また、微生物は一般に水温や溶存酸素などの環境が整った上で、好む餌などが充足されないと増殖しない。従って、バチルス菌に優占化されていない生物処理槽に当該菌を添加しても、バチルス菌が増殖し優占化状態となることは難しい。
そこで、バチルス菌を培養する為の槽を新しく設け、該槽で培養されたバチルス菌を定期的に生物処理槽へ移送する方法が提案されている(特許文献6)。しかしながら、新設した槽内でバチルス菌を培養するには、バチルス菌の増殖に適した環境を整えると共に、好む餌を与え続けなければならないので、煩雑であるだけでなく費用もかさむという欠点があった。係る欠点は、汚泥中のバチルス菌以外の微生物群を選択的に死滅させた生物処理槽で汚水処理を行い、前記バチルス菌を増殖させて優占化させることによって改善される(特許文献7)ものの、高い効率で安定に稼働させる安価な方法は未だ知られていなかった。
そこで本発明者等は、汚泥中のバチルス属以外の細菌群をより効率的に死滅させることについて鋭意検討した結果、同一の汚泥可溶化装置で2回以上処理すること、および最初の処理時には空気を供給せず最後の処理時に空気を供給することによって、バチルス属を主体とする細菌群(以下、バチルス菌等とする)およびそれらの胞子以外の微生物群の細胞を効率よく破壊し、これらの微生物群を容易に可溶化することができると共に、バチルス菌等を優占化することも容易であり、この、バチルス菌等の優占化を利用することが有機性排水の処理に有効であることを見いだし、本発明に到達した。
従って本発明の第1の目的は、微生物を含有する汚泥を効率よく可溶化するための簡便な方法を提供することにある。
本発明の第2の目的は、バチルス菌等の優占化を容易に実現することのできる方法を提供することにある。
更に本発明の第3の目的は、上記バチルス菌等の優占化を利用した、優れた、有機性排水の処理方法を提供することにある。
Therefore, the present inventors have conducted intensive studies on more efficiently killing bacteria other than the genus Bacillus in the sludge. As a result, the inventors have treated the same sludge solubilizer twice or more, and the first treatment is air. By supplying air at the time of the last treatment without supplying the bacteria, cells of bacteria group mainly composed of Bacillus (hereinafter referred to as Bacillus etc.) and microorganism groups other than those spores are efficiently destroyed. It is possible to easily solubilize microbial groups, and it is also easy to dominate Bacillus bacteria, etc., and it is effective for the treatment of organic wastewater to use this dominance of Bacillus bacteria, etc. As a result, the present invention has been reached.
Accordingly, a first object of the present invention is to provide a simple method for efficiently solubilizing sludge containing microorganisms.
The second object of the present invention is to provide a method capable of easily realizing the predominance of Bacillus bacteria and the like.
Furthermore, the third object of the present invention is to provide an excellent organic wastewater treatment method utilizing the predominance of the aforementioned Bacillus bacteria and the like.
本発明の上記の諸目的は、微生物を含有する汚泥流体を開口から高速で噴出させ、前記汚泥流体中にキャビテーションを発生させることによって前記微生物を可溶化する方法であって、前記噴出が、前記流体の噴出口と排出口およびこれらの間に設けられたキャビテーション発生室、並びに、該キャビテーション発生室の内側に設けられた空気供給孔を有する汚泥可溶化装置内に、2サイクル以上なされると共に、最初のサイクルでは前記空気供給孔からの空気の供給がなされず最後のサイクルで空気が供給されることを特徴とする汚泥の減量化方法、バチルス属を主体とする細菌群の優占化方法、及び、該優占化方法を用いた有機性排水の処理方法によって達成された。
本発明においては、特に前記噴出時の汚泥流体の温度が40℃以上であることが好ましく、噴出時の汚泥流体のpHは10.5以上であることが好ましい。
更に、前記バチルス菌等及び/またはその胞子を多量に含む流体を、生物処理槽に戻して有機性排水を処理する場合には、生物処理槽の前段に設けた流量調整槽を介して戻すことが好ましく、また、その戻し工程の途中に前記バチルス菌等および/又はその胞子を増殖・優占化させる育成槽を設けることが好ましく、前記流量調整槽、生物処理槽および育成槽の少なくとも1つの槽に、前記バチルス菌等および/又はその胞子を培養するための栄養源を供給することが好ましい。この場合、育成槽の温度を5〜40℃に制御することが好ましい。
The above-mentioned objects of the present invention are a method of solubilizing microorganisms by causing a sludge fluid containing microorganisms to be ejected from an opening at high speed and generating cavitation in the sludge fluid, wherein the ejection is performed as described above. In the sludge solubilizer having two or more fluid outlets and outlets, a cavitation generation chamber provided between them, and an air supply hole provided inside the cavitation generation chamber, two or more cycles are performed, In the first cycle, air is not supplied from the air supply hole but air is supplied in the last cycle, a method for reducing sludge, a method for predominating a bacterial group mainly composed of Bacillus, And it achieved by the processing method of the organic waste_water | drain using this dominant method.
In the present invention, in particular, the temperature of the sludge fluid at the time of ejection is preferably 40 ° C. or higher, and the pH of the sludge fluid at the time of ejection is preferably 10.5 or higher.
Furthermore, when returning the fluid containing a large amount of the Bacillus bacteria and / or its spores to the biological treatment tank to treat organic wastewater, the fluid should be returned through a flow rate adjustment tank provided in the preceding stage of the biological treatment tank. It is preferable to provide a growth tank in which the Bacillus bacteria and / or spores thereof are proliferated / dominated during the returning step, and at least one of the flow rate adjustment tank, the biological treatment tank and the growth tank It is preferable to supply a nutrient source for culturing the Bacillus bacteria and / or the spores thereof to the tank. In this case, it is preferable to control the temperature of the growth tank to 5 to 40 ° C.
本発明によれば、生物処理槽から発生する汚泥を容易に削減しつつ、バチルス菌等の優占化も同時に行えるので、これを利用して、有機性排水を従来以上に効率的に処理することができる。即ち、バチルス菌等を優占化させた結果、処理水質の向上、悪臭の抑制、余剰汚泥の減少に伴う汚泥の可溶化装置稼働時間の短縮が達成されると共に、有機性排水処理施設の維持管理が容易になるので、そのコストも低減される。 According to the present invention, the sludge generated from the biological treatment tank can be easily reduced and the dominance of Bacillus bacteria can be performed at the same time, so that the organic wastewater can be treated more efficiently than before. be able to. That is, as a result of dominating Bacillus bacteria, etc., it is possible to improve the quality of treated water, suppress bad odor, shorten the sludge solubilizer operation time due to excess sludge reduction, and maintain organic wastewater treatment facilities Since management becomes easy, the cost is also reduced.
本発明の微生物を含有する汚泥の可溶化方法は、微生物を含有する流体を開口部から高速で噴出させることによって微生物の細胞を破壊することにより、該微生物を可溶化する方法に属する。上記噴出は、流体の噴出口と排出口およびこれらの間に設けられたキャビテーション発生室、並びに、該キャビテーション発生室の内側に設けられた空気供給孔を有する汚泥可溶化装置内になされる。このような汚泥可溶化装置としては、特開2005−28306号公報に記載された汚水浄化装置、および、これと類似した装置を適宜使用することが出来る。 The method for solubilizing sludge containing microorganisms of the present invention belongs to a method for solubilizing microorganisms by destroying the cells of microorganisms by ejecting a fluid containing microorganisms from an opening at high speed. The ejection is performed in a sludge solubilizer having a fluid ejection port and a discharge port, a cavitation generation chamber provided therebetween, and an air supply hole provided inside the cavitation generation chamber. As such a sludge solubilizing device, a sewage purification device described in JP-A-2005-28306 and a similar device can be used as appropriate.
本発明では、特に、処理する汚泥流体を少なくとも2回、同じ汚泥可溶化装置から噴出させる。即ち、一度噴出させた汚泥流体を再度同じ汚泥可溶化装置に導入し、再度噴出させるという操作を繰り返す点に本発明の第1の特徴がある。この場合、噴出回数が2回であれば2サイクル、3回であれば3サイクルというように、噴出回数をサイクル数と定義する。 In the present invention, in particular, the sludge fluid to be treated is ejected from the same sludge solubilizer at least twice. That is, the first feature of the present invention is that the sludge fluid once ejected is again introduced into the same sludge solubilizer and is ejected again. In this case, the number of ejections is defined as the number of cycles, such as 2 cycles if the number of ejections is 2 and 3 cycles if the number is 3.
本発明の第2の特徴は、最初のサイクルでは空気を供給せず、最後のサイクルで空気を供給する点にある。それ以外のサイクルでは、設計によって空気を供給する場合も供給しない場合もある。汚泥可溶化装置は、空気を供給せずに汚泥流体を噴出させると汚泥流体にキャビテーションが発生するように、噴出量より排出口からの排出量が多くなるように設計される。即ち、キャビテーション発生室は減圧となっているのでキャビテーションが発生しやすくなる。このキャビテーションによって微生物の細胞膜や細胞壁が破壊され、微生物が可溶化される。本発明の汚泥可溶化装置は、汚泥の目詰まりが発生しないように、噴出口の直径を6mm程度以上としても微生物を可溶化することができるが、特に本発明では可溶化を十分に行うために、少なくとも2回噴出させる。 The second feature of the present invention is that air is not supplied in the first cycle but air is supplied in the last cycle. In other cycles, air may or may not be supplied depending on the design. The sludge solubilization device is designed so that the discharge amount from the discharge port is larger than the discharge amount so that cavitation occurs in the sludge fluid when the sludge fluid is jetted without supplying air. That is, since the cavitation generation chamber is decompressed, cavitation is likely to occur. This cavitation destroys the cell membrane and cell wall of the microorganism and solubilizes the microorganism. The sludge solubilization apparatus of the present invention can solubilize microorganisms even when the diameter of the jet outlet is about 6 mm or more so that sludge clogging does not occur. In particular, the present invention sufficiently performs solubilization. And squirt at least twice.
空気を供給せずに汚泥流体を噴出させる場合には密閉系で行われ、空気を供給する場合には、前記空気供給孔に設けられた、例えば電磁バルブを開口すれば良い。噴出後の汚泥流体を再度汚泥可溶化装置に導入するために、必要であればバッファー槽を設けても良い。噴出後の汚泥流体を再サイクルさせるか生物処理槽に戻すかの岐路には、三方弁を1個または二方弁を2個配置する。これらの弁は、電磁弁とすることが好ましい。 When the sludge fluid is ejected without supplying air, it is performed in a closed system. When air is supplied, for example, an electromagnetic valve provided in the air supply hole may be opened. In order to introduce the sludge fluid after ejection into the sludge solubilizer again, a buffer tank may be provided if necessary. One or more two-way valves or two two-way valves are arranged at the crossroads of recirculating the sludge fluid after ejection or returning it to the biological treatment tank. These valves are preferably solenoid valves.
本発明においては、微生物の可溶化を促進するために、噴出時の汚泥流体のpHを10.5以上とすることが好ましく、特にpHを11以上とすることが好ましい。このpHの調整は、公知のアルカリを用いて行えば良いが、通常は安価なナトリウム塩又はカルシウム塩を使用する。また、上記微生物の可溶化の促進は、上記pHの調節と共に、あるいはpHの調節に替えて、噴出前の汚泥流体を加熱することによって行うことができる。特に、噴出前の汚泥流体の温度を40℃以上にした場合には、バチルス菌等以外の細菌が死滅し、バチルス菌等および/またはそれらの胞子が生き残るので、有機性排水の浄化に特に有効なバチルス菌等を選択的に優占化させることができる。
因みに、バチルス菌等は容易に胞子となって、衝撃やアルカリ、あるいは高温に耐えることができるので、本発明の方法によって容易にバチルス菌等を優占化することができる。
In the present invention, in order to promote the solubilization of microorganisms, the pH of the sludge fluid at the time of ejection is preferably 10.5 or more, and particularly preferably 11 or more. The pH may be adjusted using a known alkali, but usually an inexpensive sodium salt or calcium salt is used. In addition, the solubilization of the microorganism can be promoted by heating the sludge fluid before jetting together with the pH adjustment or in place of the pH adjustment. In particular, when the temperature of the sludge fluid before jetting is 40 ° C. or higher, bacteria other than Bacillus bacteria and the like are killed, and Bacillus bacteria and / or their spores survive, which is particularly effective for purification of organic waste water. It is possible to make dominant Bacillus and the like selectively dominant.
Incidentally, Bacillus bacteria and the like can easily become spores and can withstand impact, alkali, or high temperature, and therefore Bacillus bacteria and the like can be easily dominated by the method of the present invention.
本発明においては、前記汚泥中のバチルス菌等以外の微生物群を選択的に可溶化させた汚泥流体を、前記生物処理槽で再度生物処理するが、可溶化した微生物の死骸である細胞壁や細胞膜はバチルス菌等の餌となるので、前記生物処理槽内でバチルス菌等を増殖・優占化させることができる。しかしながら、生物処理槽に戻す汚泥可溶化装置から排出されたばかりの汚泥流体にはバチルス菌等の胞子が多いので、生物処理槽に投入される前に、上記胞子を育成し、バチルス菌等を優占化させることが好ましい。そのために、本発明では可溶化処理後の汚泥流体を直接生物処理槽に戻すのではなく、生物処理槽の前に通常設けられる流量調整槽を介して生物処理槽に戻すことが好ましい。この場合、流量調整槽はバチルス菌等の育成槽として機能することになる。 In the present invention, the sludge fluid in which microorganisms other than Bacillus bacteria and the like in the sludge are selectively solubilized is biologically treated again in the biological treatment tank, but cell walls and cell membranes which are dead bodies of solubilized microorganisms Is a bait for Bacillus, etc., so that Bacillus can be proliferated and predominated in the biological treatment tank. However, since the sludge fluid just discharged from the sludge solubilizer to be returned to the biological treatment tank contains many spores such as Bacillus bacteria, the above spores are grown before being put into the biological treatment tank, and the Bacillus bacteria and the like are favored. It is preferable to make it occupied. Therefore, in the present invention, it is preferable that the sludge fluid after the solubilization treatment is not directly returned to the biological treatment tank, but is returned to the biological treatment tank through a flow rate adjustment tank that is usually provided in front of the biological treatment tank. In this case, the flow rate adjustment tank functions as a growth tank for Bacillus bacteria or the like.
本発明においては、上記流量調整槽と共に、又は流量調整槽に替えて、前記可溶化処理後の汚泥流体の戻し工程の途中に、別途育成槽を設けても良い。前記育成槽として機能する流量調整槽を含む育成槽の温度は、バチルス菌等の増殖に適した5〜40℃とすることが好ましく、また、可溶化した微生物の死骸だけでは不足する栄養素を補給することが好ましい。育成槽は、必要に応じて中和処理される。 In this invention, you may provide a separate growth tank in the middle of the return process of the sludge fluid after the said solubilization process with the said flow volume adjustment tank or replacing with a flow volume adjustment tank. The temperature of the growth tank including the flow rate adjustment tank functioning as the growth tank is preferably 5 to 40 ° C. suitable for the growth of Bacillus bacteria, etc., and supplements nutrients that are insufficient with only the dead bodies of solubilized microorganisms. It is preferable to do. The growing tank is neutralized as necessary.
また、本発明で使用する生物処理槽は好気性の曝気槽であるが、その槽は単槽である必要はなく、また、浮遊式活性汚泥、接触濾床、流動担体を用いた処理法など、有機性排水を生物処理する方式であれば特に限定されるものではない。前記生物処理槽が多槽である場合には、最初の槽の容積を小さくしておくことにより、この槽に育成槽としての機能を持たせることも出来る。 In addition, the biological treatment tank used in the present invention is an aerobic aeration tank, but the tank does not need to be a single tank, and also includes a floating activated sludge, a contact filter bed, a treatment method using a fluid carrier, etc. The organic wastewater is not particularly limited as long as it is a biological treatment system. When the biological treatment tank is a multi-tank, it is possible to give the tank a function as a growth tank by reducing the volume of the first tank.
以下、本発明を図面に基づいて更に説明する。
図1は、本発明の有機性排水処理方法を説明する概念図である。図において、有機性排水1は生物処理槽2へ送られ、生物処理される。処理された有機性排水1は、沈殿槽や膜分離槽等の固液分離槽3に送られて固液分離され、上澄水と沈降した汚泥とに分けられる。前記上澄水は処理水4として系外へ排出され、沈降した汚泥は、返送汚泥5と余剰汚泥6とに分けられ、返送汚泥5は汚泥可溶化装置7によって可溶化処理され、可溶化処理後の汚泥流体8は、必要に応じて設けられた育成槽を経由して生物処理槽2または該生物処理槽の前に設けられた流量調整槽(図示せず)へ返送され、余剰汚泥6は系外へ排出される。
Hereinafter, the present invention will be further described with reference to the drawings.
FIG. 1 is a conceptual diagram illustrating the organic wastewater treatment method of the present invention. In the figure, organic waste water 1 is sent to a biological treatment tank 2 and biologically treated. The treated organic waste water 1 is sent to a solid-liquid separation tank 3 such as a sedimentation tank or a membrane separation tank for solid-liquid separation, and divided into supernatant water and sedimented sludge. The supernatant water is discharged out of the system as treated water 4, and the settled sludge is divided into return sludge 5 and surplus sludge 6. Return sludge 5 is solubilized by sludge solubilizer 7, and after solubilization treatment The sludge fluid 8 is returned to the biological treatment tank 2 or a flow rate adjustment tank (not shown) provided in front of the biological treatment tank via a growth tank provided as necessary. It is discharged out of the system.
バチルス菌には、活性汚泥に含有される、通常の微生物には分解しにくいといわれる可溶化された細胞壁や細胞膜を餌として増殖する能力がある。したがって、上記のように可溶化処理された汚泥流体を、必要に応じて設けた育成槽を介して生物処理槽2または該生物処理槽の前に設けられた流量調整槽(図示せず)に返送することにより、生物処理槽2内がバチルス菌等によって優占化される結果、有機性排水が、バチルス菌等によって悪臭を発生することなく、効率よく処理される。 Bacillus bacteria have the ability to grow by using solubilized cell walls and cell membranes, which are contained in activated sludge and are not easily decomposed by normal microorganisms. Therefore, the sludge fluid solubilized as described above is supplied to the biological treatment tank 2 or a flow rate adjustment tank (not shown) provided in front of the biological treatment tank via a growth tank provided as necessary. By returning, the inside of the biological treatment tank 2 is dominated by Bacillus bacteria and the like, so that the organic wastewater is efficiently treated without causing malodor due to Bacillus bacteria and the like.
上記したように、バチルス菌等は、臭気成分を分解する能力を有しているので、排水処理時のDO(溶存酸素)が低い条件のときに発生する、アンモニアや硫化水素などの悪臭の原因となる成分を分解するため、有機性排水処理時に発生することのある悪臭も抑制される。 As mentioned above, Bacillus bacteria and the like have the ability to decompose odor components, and thus cause odors such as ammonia and hydrogen sulfide that are generated under conditions of low DO (dissolved oxygen) during wastewater treatment. In order to decompose the component which becomes, the malodor which may generate | occur | produce at the time of organic waste water treatment is also suppressed.
また、有機性排水1にでん粉や脂肪などが多く含まれている場合には、通常の生物処理ではこれらを分解・除去する微生物が少ないため、未処理のまま処理水4に含まれることが多いが、バチルス菌等は、これらのでん粉や脂肪を分解・除去する能力を有しているので、処理水4の水質を向上させることができる。 Further, when the organic waste water 1 contains a large amount of starch, fat and the like, it is often contained in the treated water 4 as it is untreated because there are few microorganisms that decompose and remove these in a normal biological treatment. However, since Bacillus bacteria have the ability to decompose and remove these starches and fats, the quality of the treated water 4 can be improved.
本発明によれば、生物処理槽から発生する汚泥を容易に削減しつつ、バチルス菌等の優占化も同時に行えるので、これを利用して、有機性排水を従来以上に効率的に処理することができる。即ち、バチルス菌等を優占化させた結果、処理水質の向上、悪臭の抑制、余剰汚泥の減少に伴う汚泥の可溶化装置稼働時間の短縮が達成されると共に、有機性排水処理施設の維持管理が容易になり、そのコストも低減されるので産業上極めて有意義である。 According to the present invention, the sludge generated from the biological treatment tank can be easily reduced and the dominance of Bacillus bacteria can be performed at the same time, so that the organic wastewater can be treated more efficiently than before. be able to. That is, as a result of dominating Bacillus bacteria, etc., it is possible to improve the quality of treated water, suppress bad odor, shorten the sludge solubilizer operation time due to excess sludge reduction, and maintain organic wastewater treatment facilities Since management becomes easy and the cost is reduced, it is very significant in industry.
1 有機性排水
2 生物処理槽
3 固液分離槽
4 処理水
5 返送汚泥
6 余剰汚泥
7 汚泥可溶化装置
8 可溶化処理後の汚泥流体
DESCRIPTION OF SYMBOLS 1 Organic waste water 2 Biological treatment tank 3 Solid-liquid separation tank 4 Treated water 5 Return sludge 6 Excess sludge 7 Sludge solubilizer 8 Sludge fluid after solubilization treatment
Claims (13)
The method for treating organic waste water according to claim 11 or 12, wherein the temperature of the growth tank is controlled to 5 to 40 ° C.
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JP2003010890A (en) * | 2001-07-06 | 2003-01-14 | Yanmar Co Ltd | Sludge solubilization method, sludge solubilization apparatus and drainage treating system provided with the same |
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