JP4915054B2 - Organic wastewater treatment equipment - Google Patents
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- JP4915054B2 JP4915054B2 JP2005107275A JP2005107275A JP4915054B2 JP 4915054 B2 JP4915054 B2 JP 4915054B2 JP 2005107275 A JP2005107275 A JP 2005107275A JP 2005107275 A JP2005107275 A JP 2005107275A JP 4915054 B2 JP4915054 B2 JP 4915054B2
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- 238000004065 wastewater treatment Methods 0.000 title claims description 23
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 170
- 239000002351 wastewater Substances 0.000 claims description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 238000001914 filtration Methods 0.000 claims description 16
- 239000010815 organic waste Substances 0.000 claims description 11
- 238000001556 precipitation Methods 0.000 claims description 8
- 230000015271 coagulation Effects 0.000 claims description 6
- 238000005345 coagulation Methods 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 5
- 239000005416 organic matter Substances 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 230000002776 aggregation Effects 0.000 claims description 2
- 238000004220 aggregation Methods 0.000 claims description 2
- 238000005189 flocculation Methods 0.000 claims description 2
- 230000016615 flocculation Effects 0.000 claims description 2
- 230000001376 precipitating effect Effects 0.000 claims description 2
- 244000005700 microbiome Species 0.000 description 11
- 239000000701 coagulant Substances 0.000 description 7
- 239000004744 fabric Substances 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 230000008929 regeneration Effects 0.000 description 5
- 238000011069 regeneration method Methods 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- 239000004576 sand Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- -1 carrier Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000725 suspension 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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- Biological Treatment Of Waste Water (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Filtration Of Liquid (AREA)
Description
本発明は、有機性排水の処理装置、特に活性炭を使用した処理装置に関するものである。 The present invention relates to an organic wastewater treatment apparatus, and more particularly to a treatment apparatus using activated carbon.
活性炭の吸着作用を利用する排水処理法は、排水中の各種溶存汚濁物質を除去するための最も簡便な処理方法として広く用いられている。 The wastewater treatment method using the adsorption action of activated carbon is widely used as the simplest treatment method for removing various dissolved pollutants in the wastewater.
従来、このような活性炭を用いた吸着塔は、一般的な排水処理システムの中では、SS(懸濁物質)を濾過装置で除去後、高度処理設備として用いられていた(例えば、特許文献1参照)。なお、SS(Suspended Solid)とは、当該技術分野において一般に使用される用語であり、例えば、水中に浮遊して、溶解しない物質の総称であって、1L中の乾燥重量(mg)で表される。 Conventionally, an adsorption tower using such activated carbon has been used as an advanced treatment facility after removing SS (suspended material) with a filtration device in a general wastewater treatment system (for example, Patent Document 1). reference). SS (Suspended Solid) is a term generally used in the technical field, and is a general term for substances that float in water and do not dissolve, for example, expressed in dry weight (mg) in 1 L. The
また、有機性汚濁物質を含む排水を好気性条件下で処理する場合には、活性炭の表面に微生物が着生し、活性炭による汚濁物質吸着作用と、着生微生物による吸着有機物の酸化分解作用とが併行して行われ、活性炭の活性は微生物により再生され、長期に渡り維持されるようになる。この現象は、活性炭の生物再生作用として知られている。 In addition, when wastewater containing organic pollutants is treated under aerobic conditions, microorganisms grow on the surface of activated carbon, and the pollutant adsorption action by activated carbon and the oxidative decomposition action of adsorbed organic substances by the settled microorganisms The activity of activated carbon is regenerated by microorganisms and is maintained for a long time. This phenomenon is known as the biological regeneration action of activated carbon.
この活性炭による生物再生作用を利用する排水処理装置としては、例えば粒状活性炭を層状に充填して吸着塔とし濾過器と同様に活性炭層に処理すべき排水を上向流で通水し、活性炭を流動化状態に維持する装置が実用化されている。 As a wastewater treatment device that utilizes the bioregenerative action of this activated carbon, for example, granular activated carbon is packed in layers and used as an adsorption tower. An apparatus for maintaining a fluidized state has been put into practical use.
このように上向流で通水した場合、増殖、成長した前記着生微生物が活性炭から剥離し、処理水に混ざって排出されることがあった。、そのため、上記工程の順序を逆にし、吸着工程後、濾過工程を行う処理方法も提案されている(例えば、特許文献2参照)。 In this way, when the water is passed in an upward flow, the grown and grown epiphytic microorganisms may be detached from the activated carbon and mixed with the treated water and discharged. For this reason, a processing method is also proposed in which the order of the above steps is reversed and a filtration step is performed after the adsorption step (see, for example, Patent Document 2).
この処理方法は、浄水処理方法で、粒状活性炭層に上向流で通水し、塩素添加後、急速濾過を行うもので、特にトリハロメタンを対象とするものである。 This treatment method is a water purification treatment method in which water is passed through a granular activated carbon layer in an upward flow, and after rapid addition of chlorine, rapid filtration is performed, particularly for trihalomethanes.
排水処理装置としては、完全な上向流ではないが、活性炭等の担体を使用し、処理後濾過する装置が提案されている(例えば、特許文献3参照)。 As a wastewater treatment apparatus, an apparatus that uses a carrier such as activated carbon and performs filtration after treatment has been proposed (for example, see Patent Document 3), although it is not a complete upward flow.
この特許文献3に記載された装置は、上向流路を構成する曝気槽内には微生物が付着できる活性炭等の担体が投入されており、排水、担体、空気の三層が密な接触を繰返しながら上昇するようにしてある。担体は流動状態に維持されており、処理物を吸着した担体は微生物により再生される(生物再生作用)。
In the device described in
この処理水は配管を介して次段の濾過装置に導入される。濾過には目開きが処理水中の懸濁物より小さい濾布(マイクロスクリーン)を用いている。この濾布が濾過筒に巻かれ、モータ、減速機により回転させるようになっている。 This treated water is introduced into the next-stage filtration device through a pipe. For the filtration, a filter cloth (microscreen) whose mesh opening is smaller than the suspension in the treated water is used. This filter cloth is wound around a filter cylinder and rotated by a motor and a speed reducer.
処理水は濾過筒の内側から、濾布で濾過されて、出口室に入り、ここから排出されるようになっている。また、濾過筒の上方には、洗浄ノズルが配置され、そのノズルから洗浄流体を濾布に吹き付け、その濾布面を洗浄するようにしている。 The treated water is filtered with a filter cloth from the inside of the filter tube, enters the outlet chamber, and is discharged from here. A cleaning nozzle is disposed above the filter cylinder, and a cleaning fluid is sprayed from the nozzle onto the filter cloth to clean the filter cloth surface.
この装置の特徴は、凝集剤などの水処理薬剤を使用せずに、濾過水質を向上させることができるとしている。
しかしながら、このような排水処理装置では、目開きを小さくしているため、駆動部が必要等、装置が複雑になると共に、目詰まり防止のため、濾布の洗浄頻度も多くなるという問題があった。 However, such a wastewater treatment apparatus has a problem that since the opening is made small, the drive becomes necessary and the apparatus becomes complicated, and the frequency of washing the filter cloth increases to prevent clogging. It was.
また、活性炭同士の接触により、発生する黒粉の除去は考慮されておらず、除去するためには、上記スクリーンの目開きをより小さくしなければならず、上記の問題がより大きくなるという問題があった。 Moreover, the removal of the black powder generated due to the contact between the activated carbons is not taken into consideration, and in order to remove it, the opening of the screen must be made smaller, and the above problem becomes larger. was there.
そこで、本発明は、簡単な装置で、処理水質の向上を実現する有機性排水処理装置を提供することを目的とする。 Then, an object of this invention is to provide the organic waste water treatment apparatus which implement | achieves the improvement of a treated water with a simple apparatus.
前記目的を達成するために、本発明の有機性排水処理装置は、内部に活性炭を充填し、排水を上向流で通水する上向流式活性炭塔と、その上向流式活性炭塔で処理した処理排水に凝集剤を添加する凝集剤添加手段と、前記凝集剤を添加した処理排水を濾過処理する凝集濾過器とを含み、排水中に含まれる金属あるいは有機物を沈殿・除去する開放式の沈殿槽を前記上向流式活性炭塔の上流側に配し、前記沈殿槽の上部周囲に越流槽を設け、前記越流槽の下部と前記上向流式活性炭塔の下部を配管接続し、前記沈殿槽の水位より前記上向流式活性炭塔の水位を低くした構成としている。 In order to achieve the above object, the organic waste water treatment apparatus of the present invention includes an upward activated carbon tower that is filled with activated carbon and allows waste water to flow upward, and an upward activated carbon tower. a coagulant adding means for adding a flocculant to the treated wastewater, seen including a coagulation filter to the added raw wastewater the flocculant is filtered process, precipitated and removed metal or organic substances contained in the waste water released A settling tank is arranged upstream of the upward flow activated carbon tower, an overflow tank is provided around the upper part of the precipitation tank, and a lower part of the overflow tank and a lower part of the upward activated carbon tower are piped. It connects and it is set as the structure which made the water level of the said upward flow type activated carbon tower lower than the water level of the said precipitation tank .
本構成により、凝集剤の添加により上向流式活性炭塔から排出された懸濁物質の粒径が大きくなり、簡単な構造の凝集濾過器で、その懸濁物質を除去でき、また、上向流式活性炭塔に導入される排水には、溶存酸素が多く含まれており、そのため、上向流式活性炭塔の内部では、好気性微生物が活性炭の表面に着生しやすく、この微生物により、排水中に含まれる、活性炭に吸着された有機物は酸化分解され、このように、活性炭の生物再生作用により、活性炭を取出し、再生する必要はなく、活性炭の寿命を延ばすことができる。 With this configuration, the particle size of the discharged suspended solids from upflow activated carbon column by addition of the agent is increased, in aggregate filter of simple structure, you can remove the suspended matter, also, upward The wastewater introduced into the flow activated carbon tower contains a large amount of dissolved oxygen. Therefore, inside the upward flow activated carbon tower, aerobic microorganisms tend to settle on the surface of the activated carbon. contained in the wastewater, organic matter adsorbed by the activated carbon is oxidized and decomposed, thus, the biological regeneration action of the activated carbon, extraction of activated carbon need not be reproduced, Ru can extend the life of the activated carbon.
このように、本発明の有機性排水処理装置によれば、上向流式活性炭塔に導入される排水には、溶存酸素が多く含まれており、上向流式活性炭塔特有の、活性炭の生物再生作用を利用しつつ、排出される黒粉を除去できる。すなわち、活性炭の生物再生により寿命が延びるとともに、処理水質の向上が図られる。 As described above, according to the organic waste water treatment apparatus of the present invention, the waste water introduced into the upward flow activated carbon tower contains a large amount of dissolved oxygen . The discharged black powder can be removed while utilizing the biological regeneration action. That is, the life of the activated charcoal is extended and the quality of the treated water is improved.
本発明の有機性排水処理装置は、内部に活性炭を充填し、排水を上向流で通水する上向流式活性炭塔と、その上向流式活性炭塔で処理した処理排水に凝集剤を添加する凝集剤添加手段と、前記凝集剤を添加した処理排水を濾過処理する凝集濾過器とを含み、排水中に含まれる金属あるいは有機物を沈殿・除去する開放式の沈殿槽を前記上向流式活性炭塔の上流側に配し、前記沈殿槽の上部周囲に越流槽を設け、前記越流槽の下部と前記上向流式活性炭塔の下部を配管接続し、前記沈殿槽の水位より前記上向流式活性炭塔の水位を低くした構成としている。上向流式活性炭塔に導入される排水には、溶存酸素が多く含まれており、そのため、上向流式活性炭塔の内部では、好気性微生物が活性炭の表面に着生しやすく、この微生物により、排水中に含まれる、活性炭に吸着された有機物は酸化分解され、このように、活性炭の生物再生作用により、活性炭を取出し、再生する必要はなく、活性炭の寿命を延ばすことができる。また、この凝集剤添加により、従来の凝集濾過器で微細粒子の黒粉も除去できる。また、前段に沈殿槽があるため、上向流式活性炭塔の処理負荷を低減できる。また、沈殿槽からの排出水を、ポンプ塔の動力源を使用せず、上向流式活性炭塔の出口まで、流出させることができる。 The organic waste water treatment apparatus of the present invention is filled with activated carbon inside, and an upward flow type activated carbon tower for passing the waste water in an upward flow, and a coagulant in the treated waste water treated by the upward flow type activated carbon tower. a coagulant adding means for adding the additives were treated wastewater coagulants saw including a flocculation filter for filtering process, a sedimentation tank of the open precipitating and removing the metal or organic substances contained in the waste water the upward Arranged upstream of the flow activated carbon tower, provided an overflow tank around the upper part of the settling tank, piped the lower part of the overflow tank and the lower part of the upward flow activated carbon tower, the water level of the precipitation tank Furthermore, it is set as the structure which made the water level of the said upward flow type activated carbon tower low . The wastewater introduced into the upward flow activated carbon tower contains a large amount of dissolved oxygen, and therefore, the aerobic microorganisms tend to settle on the surface of the activated carbon inside the upward flow activated carbon tower. As a result, the organic matter adsorbed on the activated carbon contained in the wastewater is oxidatively decomposed. Thus, it is not necessary to take out and regenerate the activated carbon by the bioregenerative action of the activated carbon, thereby extending the life of the activated carbon. In addition, the addition of the flocculant can also remove fine particles of black powder with a conventional flocculant filter. Moreover, since there is a settling tank in the previous stage, the processing load of the upward flow activated carbon tower can be reduced. Further, the discharged water from the settling tank can be discharged to the outlet of the upward flow activated carbon tower without using the power source of the pump tower.
また、本発明の有機性排水処理装置は、上向流式活性炭塔の内部に排水の流れを均一にする整流手段を備えることが好ましい。この整流手段により塔内の排水の流れを均一にすることで、排水と活性炭との接触効率を向上できるとともに、活性炭の流出も防止できる。 Moreover, it is preferable that the organic waste water treatment apparatus of this invention is equipped with the rectification | straightening means which makes the flow of waste water uniform in the inside of an upward flow type activated carbon tower. By making the flow of the waste water in the tower uniform by this rectifying means, the contact efficiency between the waste water and the activated carbon can be improved, and the outflow of the activated carbon can be prevented.
また、本発明の有機性排水処理装置は、上向流式活性炭塔内下部に空気による撹拌手段を備えることが好ましい。この撹拌手段により活性炭塔内を撹拌することで、活性炭表面で増殖し、剥離した着生微生物が下部に堆積するのを防ぐことができる。 Moreover, it is preferable that the organic waste water treatment apparatus of this invention is equipped with the stirring means by air in the lower part in an upward flow type activated carbon tower. By stirring the inside of the activated carbon tower with this stirring means, it is possible to prevent epiphytic microorganisms that have grown on the surface of the activated carbon and have peeled off from accumulating in the lower part.
また、本発明の有機性排水処理装置は、凝集濾過器が上向流式であることが好ましい。
上向流式は、下向流式に比べ、濾過時間が長くなり、濾過効率を向上できる。
In the organic waste water treatment apparatus of the present invention, the coagulation filter is preferably an upward flow type.
The upward flow type has a longer filtration time than the downward flow type, and can improve the filtration efficiency.
また、本発明の有機性排水処理装置は、凝集濾過器が濾材を洗浄する洗浄手段を備えることが好ましい。この洗浄手段により適時洗浄することにより、濾過効率を維持することができる。 Moreover, it is preferable that the organic waste water treatment apparatus of this invention is equipped with the washing | cleaning means in which a coagulation filter wash | cleans a filter medium. Filtration efficiency can be maintained by timely washing with this washing means.
以下に、本発明の有機性排水処理装置について例をあげて説明するが、本発明はこれに限定されるものではない。 Hereinafter, the organic wastewater treatment apparatus of the present invention will be described by way of example, but the present invention is not limited to this.
(実施例1)
図1において、上向流式活性炭塔1は、内部に活性炭2、整流手段(邪魔板)3、撹拌手段4を備え、排水は下部から導入、上部から排出、いわゆる上向流で活性炭2と接触している。上向流式活性炭塔1から排出された処理排水は、配管5を通り、凝集濾過器6へ導入される。処理排水は配管5の途中で、凝集剤添加手段7により、凝集剤が添加され、凝集濾過器6により、処理排水内のSSを除去する。凝集濾過器6内の上部には洗浄手段8が設けられており、砂等の濾過材を洗浄、再生する。活性炭2として、一般に粒状が使用されるが、繊維状活性炭の成形物も使用でき、凝集剤としては、PAC(ポリ塩化アルミニウム)や硫酸バンドが使用可能である。
Example 1
In FIG. 1, an upward flow type activated
上記構成において、上向流式活性炭塔1に導入される排水には、前工程の沈殿槽は開放式のため溶存酸素が多く含まれている。そのため、上向流式活性炭塔1の内部では、好気性微生物が活性炭2の表面に着生しやすい。この微生物により、排水中に含まれる、活性炭2に吸着された有機物は酸化分解される。このように、活性炭2の生物再生作用により、活性炭2を取出し、再生する必要はなく、活性炭2の寿命を延ばすことができる。
In the above configuration, the wastewater introduced into the upward flow activated
また、この時、上向流で、活性炭2を流動状態にするため、活性炭2同士の接触・擦れにより、黒粉を発生する。この黒粉を除去するため、凝集剤添加の効果を実験したデータを用いて説明する。
At this time, in order to make the activated
まず、濾過材として砂を用いた場合は、重量平均径1.97μmとなった。次に、濾過材として砂より微細なアンスラサイトを用いた場合でも、重量平均径1.42μmであった。そして、本実施例の砂濾材で凝集剤を併用した場合は、重量平均径0.62μmとなり、凝集剤の効果は重量平均径で約3分の1、濾過効率としては、約3倍と言える。ここで重量平均径とは、重量分布から求めた重量平均となる粒子の径で、濾過性能を評価する時には、通常用いられる粒径である。 First, when sand was used as the filter medium, the weight average diameter was 1.97 μm. Next, even when anthracite finer than sand was used as a filter medium, the weight average diameter was 1.42 μm. And when the coagulant | flocculant is used together with the sand filter medium of a present Example, it becomes a weight average diameter of 0.62 micrometer, The effect of the coagulant | flocculant is about 1/3 in a weight average diameter, and it can be said that filtration efficiency is about 3 times. . Here, the weight average diameter is a diameter of particles that is a weight average obtained from a weight distribution, and is a particle diameter that is usually used when evaluating filtration performance.
このように、上向流による活性炭の生物再生作用を利用できるとともに、濾過前に凝集剤を添加することにより、黒粉のより細かい粒子まで濾過除去できるため、濾過水の水質は向上する。 Thus, while being able to utilize the bioregenerative action of the activated carbon by the upward flow, and by adding a flocculant before filtration, finer particles of black powder can be removed by filtration, the quality of filtered water is improved.
(実施例2)
図2において、上向流式活性炭塔1の前段に、沈殿槽9が配管10を介して接続されている。また沈殿槽9の上部周囲には越流槽11が設けられ、配管10は越流槽11の下部と上向流式活性炭塔1の下部を接続しており、沈殿槽9と上向流式活性炭塔1の垂直方向の位置関係は、沈殿槽9の水位が上向流式活性炭塔1の水位より“h”高くなるように設置されている。
(Example 2)
In FIG. 2, a
上記の構成において、沈殿槽9の水位が上向流式活性炭塔1の水位より“h”高くなるように設置されているため、この“h”がヘッド差(水頭差)となり、沈殿槽9を越流した排水は、自然に越流槽11から配管10を通過し、上向流式活性炭塔1に流入し、上向流で上向流式活性炭塔1内も通過し、配管5へ流出する。
In the above configuration, since the water level in the
このように、沈殿槽9から上向流式活性炭塔1へ、ポンプ等の動力を使用せず、送水できるので、省エネが図れる。
In this way, since water can be sent from the
以上のように、本発明の有機性排水処理装置によれば、上向流式活性炭塔に導入される排水には、溶存酸素が多く含まれており、活性炭の生物再生作用を利用できるとともに、濾過水の水質も向上できるため、活性炭を利用した排水処理方法に広く利用できる。 As described above, according to the organic wastewater treatment apparatus of the present invention, the wastewater introduced into the upward flow activated carbon tower contains a large amount of dissolved oxygen, and can utilize the biological regeneration action of activated carbon. Since the quality of filtered water can be improved, it can be widely used in wastewater treatment methods using activated carbon.
1 上向流式活性炭塔
2 活性炭
3 整流手段
4 撹拌手段
5,10 配管
6 凝集濾過器
7 凝集剤添加手段
8 洗浄手段
9 沈殿槽
11 越流槽
DESCRIPTION OF
Claims (5)
その上向流式活性炭塔で処理した処理排水に凝集剤を添加する凝集剤添加手段と、
前記凝集剤を添加した処理排水を濾過処理する凝集濾過器とを含み、排水中に含まれる金属あるいは有機物を沈殿・除去する開放式の沈殿槽を前記上向流式活性炭塔の上流側に配し、前記沈殿槽の上部周囲に越流槽を設け、前記越流槽の下部と前記上向流式活性炭塔の下部を配管接続し、前記沈殿槽の水位より前記上向流式活性炭塔の水位を低くした有機性排水処理装置。 An up-flow type activated carbon tower that is filled with activated carbon and passes the waste water in an upward flow;
A flocculant addition means for adding a flocculant to the treated wastewater treated by the upward flow activated carbon tower;
Look including a flocculation filtration unit for filtration of wastewater with the addition of the flocculant, the settling tank of the open precipitating and removing the metal or organic matter contained in the wastewater upstream of the upflow activated carbon column An overflow tank is provided around the upper part of the settling tank, a lower part of the overflow tank and a lower part of the upward flow activated carbon tower are connected by piping, and the upward flow activated carbon tower from the water level of the precipitation tank Organic wastewater treatment equipment with low water level .
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