JP2009190006A - Organism desulfurization apparatus - Google Patents

Organism desulfurization apparatus Download PDF

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JP2009190006A
JP2009190006A JP2008036264A JP2008036264A JP2009190006A JP 2009190006 A JP2009190006 A JP 2009190006A JP 2008036264 A JP2008036264 A JP 2008036264A JP 2008036264 A JP2008036264 A JP 2008036264A JP 2009190006 A JP2009190006 A JP 2009190006A
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packed bed
biological desulfurization
water
tower
diffuser
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JP5269433B2 (en
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Yasuhiko Nagamori
泰彦 永森
Takumi Obara
卓巳 小原
Nobuyuki Ashikaga
伸行 足利
Hiroshi Tamura
博 田村
Takayuki Ishige
崇之 石毛
Takeo Yamamori
武夫 山森
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Toshiba Corp
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Toshiba Corp
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Priority to JP2008036264A priority Critical patent/JP5269433B2/en
Priority to CN2008800062299A priority patent/CN101622330B/en
Priority to PCT/JP2008/073880 priority patent/WO2009084699A1/en
Priority to US12/527,700 priority patent/US20100261266A1/en
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M47/00Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
    • C12M47/18Gas cleaning, e.g. scrubbers; Separation of different gases

Abstract

<P>PROBLEM TO BE SOLVED: To save trouble cleaning of a packed bed of an organism desulfurization apparatus and improve its cleaning effect. <P>SOLUTION: The organism desulfurization apparatus includes an organism desulfurization column 1 having an openable lid 2 or the like, an upper packed bed 3 and a lower packed bed 4 which are installed at the upper part and the lower part in the organism desulfurization column respectively and are each composed of a carrier and a supporting plate to support the carrier, an upper aeration device 7 and a lower aeration device 8 which are installed below the upper packed bed and the lower packed bed respectively and a drain pipe 12 with a drain valve 11 which is connected to the lower part of the organism desulfurization column. Firstly, after the lid or the like is opened with the drain valve 11 closed and water is filled up to above the upper packed bed 3, the upper packed bed 3 is cleaned by aeration with the upper aeration device 7. Secondly, after the aeration with the upper aeration device 7 is stopped and the water level is lowered to between the upper packed bed 3 and the lower packed bed 4 by opening the drain valve 11, the lower packed bed 4 is cleaned by aeration with the lower aeration device 8. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は生物脱硫装置に関し、特に下水や産業排水等の有機性排水の嫌気性消化処理で発生するバイオガスを処理する生物脱硫装置に関する。   The present invention relates to a biological desulfurization apparatus, and more particularly to a biological desulfurization apparatus that processes biogas generated in anaerobic digestion of organic wastewater such as sewage and industrial wastewater.

周知の如く、下水汚泥や生ごみといった有機性廃棄物や食品工場排水などの有機性排水の処理法として、メタン発酵処理法が多く適用されてきている。メタン発酵処理法は、有機性排水を生物反応槽に投入し、反応槽内に充填したメタン発酵細菌群により有機物を分解し、メタンガスを主成分とするバイオガスを生成すると共に、排水中の有機物を分解除去する処理法である。しかしながら、排水中にたんぱく質由来などの硫黄成分が含まれている場合、硫酸還元菌の作用により、硫黄成分が還元され、バイオガス中に硫化水素ガスが含まれる。   As is well known, a methane fermentation treatment method has been widely applied as a treatment method for organic waste such as sewage sludge and garbage and organic wastewater such as food factory wastewater. In the methane fermentation treatment method, organic wastewater is introduced into a biological reaction tank, organic matter is decomposed by the methane fermentation bacteria group filled in the reaction tank, biogas containing methane gas as a main component is generated, and organic matter in the wastewater is also generated. Is a treatment method for decomposing and removing. However, when the sulfur component such as protein is contained in the waste water, the sulfur component is reduced by the action of the sulfate reducing bacteria, and hydrogen sulfide gas is contained in the biogas.

ところで、バイオガス中に含まれるメタンガスをボイラーなどの燃料として使用する場合には、バイオガスに含まれる硫化水素ガスを除去する必要が生じる。この理由は、バイオガスを燃焼させる際にバイオガス中の硫化水素ガスが酸化されて硫黄酸化物が生成し、機器を腐食させる可能性があるためである。   By the way, when methane gas contained in biogas is used as a fuel such as a boiler, it is necessary to remove hydrogen sulfide gas contained in biogas. This is because when the biogas is burned, the hydrogen sulfide gas in the biogas is oxidized to produce sulfur oxide, which may corrode the equipment.

バイオガス中に含まれる硫化水素ガスを除去する方法としては、酸化鉄を主成分とする吸着剤を用いて吸着除去する乾式脱硫方法、あるいはアルカリなどを用いた水溶液に吸収除去する湿式脱硫方法が利用されている。しかし、これらの方法は、吸着のために吸着剤などの薬品が必要であることと、吸着後の吸着剤が廃棄物になることから、ランニングコストが高騰する方式であった。   As a method for removing hydrogen sulfide gas contained in biogas, there are a dry desulfurization method in which adsorption is performed using an adsorbent mainly composed of iron oxide, or a wet desulfurization method in which it is absorbed and removed in an aqueous solution using alkali or the like. It's being used. However, these methods are systems in which running costs increase because chemicals such as an adsorbent are required for adsorption and the adsorbent after adsorption becomes waste.

そこで、低ランニングコストで脱硫を行うシステムとして、反応槽に硫化水素を酸化分解する微生物が付着した担体を充填し、バイオガス中の硫化水素を除去する技術(特許文献1)が提案されている。
この脱硫技術においては、充填層や充填層の支持部に増殖した微生物や除去された硫化水素が酸化して生成する単体硫黄により充填層が閉塞しやすいといった問題点が指摘されている。それを解決する手段として、バイオガスを下降流に流すと共に、水より軽い担体を用い、充填層の高さ以上に水を張り、下部から空気を吹き込んで担体を水中で流動させ、洗浄する方法(特許文献2)が提案されている。
特開平2−26615号公報 特許第3750648号公報
Therefore, as a system for performing desulfurization at a low running cost, a technique (Patent Document 1) for removing hydrogen sulfide in biogas by filling a reaction tank with a carrier attached with microorganisms that oxidize and decompose hydrogen sulfide has been proposed. .
In this desulfurization technique, it has been pointed out that the packed bed is likely to be clogged by the microorganisms grown on the packed bed and the supporting part of the packed bed or by simple sulfur produced by oxidizing the removed hydrogen sulfide. As a means for solving this, a method of flowing a biogas in a downward flow, using a carrier lighter than water, spreading water above the height of the packed bed, blowing air from the lower part, causing the carrier to flow in water and washing (Patent Document 2) has been proposed.
JP-A-2-26615 Japanese Patent No. 3750648

充填層の洗浄は、単体硫黄を充填層より剥離させるために行うが、洗浄によって担体上に増殖した微生物も剥離する。即ち、洗浄を長時間行うと、単体硫黄による充填層の閉塞は改善されるものの、微生物がほとんど剥離してしまい、生物脱硫装置の硫化水素除去性能が大きく低下する。従って、洗浄は硫化水素除去性能を維持できる程度に行わなければならない。   Washing of the packed bed is performed in order to peel off elemental sulfur from the packed bed, but microorganisms grown on the carrier are also peeled off by washing. That is, when the washing is performed for a long time, the clogging of the packed bed with single sulfur is improved, but the microorganisms are almost peeled off, and the hydrogen sulfide removal performance of the biological desulfurization apparatus is greatly reduced. Therefore, the cleaning must be performed to such an extent that the hydrogen sulfide removal performance can be maintained.

そしてそれは充填層が2段である場合、特に問題となる。何故ならば、2段の充填層を備える生物脱硫装置の場合、上段と下段の充填層での単体硫黄の生成量は異なり、バイオガス中の硫化水素濃度が高い流入側に近い下段の充填層での単体硫黄の生成量が多いためである。発明者らの実験によれば、2段充填層を有する生物脱硫装置の1ヶ月の運転によって充填層に付着した単体硫黄量は、下段の充填層では上段の充填層の4〜5倍であった。この場合、2段の充填層に同じ洗浄を行うと、下段の単体硫黄が十分に剥離されないか、上段の微生物が必要量維持されない危険性がある。   And it becomes a problem especially when the packed bed has two stages. This is because in the case of a biodesulfurization apparatus having a two-stage packed bed, the amount of elemental sulfur produced in the upper and lower packed beds is different, and the lower packed bed close to the inflow side where the hydrogen sulfide concentration in biogas is high. This is because a large amount of elemental sulfur is produced in the process. According to the experiments by the inventors, the amount of elemental sulfur adhering to the packed bed after one month of operation of the biodesulfurization apparatus having a two-stage packed bed is 4 to 5 times that of the upper packed bed in the lower packed bed. It was. In this case, if the same washing is performed on the two-stage packed bed, there is a risk that the lower-stage single sulfur will not be sufficiently separated or the necessary amount of the upper-stage microorganisms will not be maintained.

また、充填層が担体と担体を支持する支持板とで構成される場合、支持板にも担体硫黄が付着して閉塞要因となるが、洗浄では、担体は水中で流動するが、支持板は固定されているため水に浸かるのみで、洗浄効果が弱い恐れがある。   Also, when the packed bed is composed of a carrier and a support plate that supports the carrier, carrier sulfur adheres to the support plate and becomes a clogging factor, but in washing, the carrier flows in water, but the support plate Since it is fixed, it may be weakened by just soaking it in water.

本発明はこうした事情を考慮してなされたもので、充填層を2段備える生物脱硫装置において、充填層の洗浄を少ない手間で行うことができるとともに、洗浄効果を高くしえる生物脱硫装置を提供することを目的とする。   The present invention has been made in consideration of such circumstances, and in a biological desulfurization apparatus having two packed beds, a biological desulfurization apparatus that can perform cleaning of the packed bed with less labor and can enhance the cleaning effect is provided. The purpose is to do.

本発明の生物脱硫装置は、以下の通りである。
(1)上部に開閉可能な蓋もしくはバルブを備えた生物脱硫塔と、この生物脱硫塔内の上下に夫々配置され,担体及び該担体を支持する支持板からなる上段充填層及び下段充填層と、これらの上段充填層及び下段充填層の下側に夫々配置された上段散気装置及び下段散気装置と、前記生物脱硫塔の下部に接続された,排水弁を介装した処理水配管とを具備した生物脱硫装置であって、前記蓋もしくはバルブを開け、前記排水弁を閉じ、前記上段充填層より上まで水によって満たした状態で、前記上段散気装置に空気を供給して曝気を行うことで前記上段充填層の洗浄を行い、その後、前記上段散気装置を停止し、前記排水弁を開け、水位を前記上段充填層より下で且つ前記下段充填層より上まで下げた状態で、前記下段散気装置に空気を供給して曝気を行うことで前記下段充填層の洗浄を行う構成であることを特徴とする生物脱硫装置(第1の発明)。
The biological desulfurization apparatus of the present invention is as follows.
(1) A biodesulfurization tower having a lid or a valve that can be opened and closed at the top, and an upper packed bed and a lower packed bed that are respectively arranged above and below the biodesulfurization tower and are composed of a support and a support plate that supports the support. An upper air diffuser and a lower air diffuser disposed below the upper packed bed and the lower packed bed, respectively, and a treated water pipe connected to the lower part of the biological desulfurization tower via a drain valve, A biological desulfurization apparatus comprising: opening the lid or valve; closing the drain valve; and filling the upper stage packed bed with water to supply air to the upper stage air diffuser for aeration. In this state, the upper packed bed is washed, and then the upper diffuser is stopped, the drain valve is opened, and the water level is lowered below the upper packed bed and above the lower packed bed. , Supply air to the lower diffuser Biological desulfurization apparatus, characterized in that the arrangement for cleaning of the lower filling layer by performing aeration Te (the first invention).

(2)上部に開閉可能な蓋もしくはバルブを備えた生物脱硫塔と、この生物脱硫塔内の上下に夫々配置され,担体及び該担体を支持する支持板からなる上段充填層及び下段充填層と、これらの上段充填層及び下段充填層の下側に夫々配置された上段散気装置及び下段散気装置と、前記生物脱硫塔の下部に接続された,排水弁を介装した処理水配管とを具備した生物脱硫装置であって、前記蓋もしくはバルブを開け、前記排水弁を閉じ、前記上段充填層又は下段充填層の支持板が浸るまで水によって満たし、上段散気装置又は下段散気装置によって曝気を行うことで上段充填層又は下段充填層の支持板の洗浄を行う構成であることを特徴とする生物脱硫装置(第2の発明)。   (2) a biological desulfurization tower provided with a lid or valve that can be opened and closed at the top, and an upper packed bed and a lower packed bed that are respectively arranged above and below the biological desulfurized tower and are composed of a carrier and a support plate that supports the carrier; An upper air diffuser and a lower air diffuser disposed below the upper packed bed and the lower packed bed, respectively, and a treated water pipe connected to the lower part of the biological desulfurization tower via a drain valve, A biological desulfurization apparatus comprising: opening the lid or valve; closing the drain valve; filling with water until the support plate of the upper packed bed or the lower packed bed is immersed; an upper diffuser or a lower diffuser A biological desulfurization apparatus (second invention), characterized in that the aeration plate is used to wash the support plate of the upper packed bed or the lower packed bed.

(3)生物脱硫塔と、この生物脱硫塔内の上下に配置された上段充填層及び下段充填層と、前記生物脱硫塔内の上部に配置された,水の散布を行うシャワーノズルと、上段充填層及び下段充填層を経由して生物脱硫塔の底部まで滴下して滞留する底部滞留水の一部を上段充填層の上部より散布する循環装置と、前記生物脱硫塔の下部に接続された,排水弁を介装した処理水配管とを具備した生物脱硫装置であって、前記上部充填層の微生物が洗浄によって過剰に剥離した場合、前記循環装置による底部滞留水の循環と前記シャワーノズルによる水の散布とを併用することにより上段充填層の微生物量を回復する構成であることを特徴とする生物脱硫装置(第3の発明)。   (3) a biological desulfurization tower, an upper packed bed and a lower packed bed disposed above and below the biological desulfurization tower, a shower nozzle for spraying water disposed at an upper portion in the biological desulfurization tower, A circulation device for spraying a part of the bottom retained water that drops and stays to the bottom of the biological desulfurization tower via the packed bed and the lower packed bed is connected to the lower part of the biological desulfurization tower. , A biological desulfurization apparatus having a treated water pipe interposing a drain valve, and when microorganisms in the upper packed bed are excessively separated by washing, circulation of bottom accumulated water by the circulation apparatus and by the shower nozzle A biodesulfurization apparatus (third invention) characterized in that the amount of microorganisms in the upper packed bed is recovered by using water spraying together.

(4)上部に開閉可能な蓋もしくはバルブを備えた生物脱硫塔と、この生物脱硫塔内の上下に夫々配置され,担体及び該担体を支持する支持板からなる上段充填層及び下段充填層と、これらの上段充填層及び下段充填層の下側に夫々配置された,高圧洗浄ノズルを有した高圧洗浄装置と、前記生物脱硫塔の下部に接続された,排水弁を介装した処理水配管とを具備した生物脱硫装置であって、前記高圧洗浄装置の高圧洗浄ノズルに水を供給することにより前記上段充填層及び下段充填層の洗浄を行う構成であることを特徴とする生物脱硫装置(第4の発明)。   (4) a biodesulfurization tower having a lid or a valve that can be opened and closed at the top, and an upper packed bed and a lower packed bed that are respectively arranged above and below the biodesulfurization tower and are composed of a support and a support plate that supports the support; , A high-pressure washing apparatus having a high-pressure washing nozzle, which is arranged below each of the upper packed bed and the lower packed bed, and a treated water pipe connected to the lower part of the biological desulfurization tower, with a drain valve A biological desulfurization apparatus comprising: a structure for cleaning the upper packed bed and the lower packed bed by supplying water to a high pressure cleaning nozzle of the high pressure cleaning apparatus ( Fourth invention).

本発明によれば、充填層の洗浄を少ない手間で行うことができるとともに、洗浄効果を高くしえる生物脱硫装置を提供できる。また、上段充填層と下段充填層の洗浄の頻度を適宜設定する等の手段を講じることにより、生物脱硫装置の硫化水素の除去性能を長期にわたって高く安定させることができる。更に、生物脱硫塔内の底部滞留水を循環させる循環装置を配置することにより、硫化水素の除去性能の低下を短期に回復することができる。更には、生物脱硫塔内の水位を容易に判断する手段を講じることにより洗浄作業を容易化でき、上段充填層や下段充填層に夫々高圧洗浄装置を設置することにより洗浄の短時間を実現できる。   According to the present invention, it is possible to provide a biodesulfurization apparatus that can clean the packed bed with less labor and can enhance the cleaning effect. Further, by taking measures such as appropriately setting the frequency of cleaning the upper packed bed and the lower packed bed, the hydrogen sulfide removal performance of the biological desulfurization apparatus can be highly stabilized over a long period of time. Furthermore, by disposing a circulation device that circulates the bottom accumulated water in the biological desulfurization tower, it is possible to recover the decrease in hydrogen sulfide removal performance in a short time. Furthermore, the cleaning operation can be facilitated by taking measures to easily determine the water level in the biological desulfurization tower, and the cleaning time can be shortened by installing high-pressure cleaning devices in the upper packed bed and the lower packed bed, respectively. .

以下、本発明に係る生物脱硫装置について更に詳しく説明する。
上記(1)の発明において、上段充填層及び下段充填層を洗浄する手段と、前記蓋若しくはバルブを開け、前記排水弁を閉じ、前記下段充填層より上まで水によって満たした状態で、前記下段散気装置によって曝気を行うことで下段充填層の洗浄を行う、下段充填層の洗浄手段を有し、下段充填層のみの洗浄の頻度を、上段充填層の洗浄の頻度より短い間隔で実施する構成であることが好ましい。
Hereinafter, the biological desulfurization apparatus according to the present invention will be described in more detail.
In the invention of the above (1), the means for cleaning the upper packed bed and the lower packed bed, the lid or valve is opened, the drain valve is closed, and the lower packed bed is filled with water up to above the lower packed bed. The lower packed bed is cleaned by aeration using an air diffuser, and the lower packed bed cleaning means is used, and the frequency of cleaning only the lower packed bed is performed at an interval shorter than the frequency of cleaning the upper packed bed. A configuration is preferred.

このような構成にする理由は次のとおりである。即ち、脱硫反応により硫化水素は硫酸もしくは単体硫黄に変化する。硫酸は排水と共に排出されるが、単体硫黄は担体に付着して上段充填層や下段充填層の閉塞因子となる。しかし、これまでの研究結果より、単体硫黄の生成は下段充填層に多いことが分かっているので、下段充填層の洗浄を上段充填層の洗浄よりも高頻度で実施すれば、上段充填層の微生物の不必要な剥離を防止して下段充填層の閉塞を抑制することができる。従って、生物脱硫装置の硫化水素の除去性能を長期にわたって高く安定させることができる。   The reason for such a configuration is as follows. That is, hydrogen sulfide changes into sulfuric acid or elemental sulfur by the desulfurization reaction. Sulfuric acid is discharged together with the waste water, but the elemental sulfur adheres to the carrier and becomes a clogging factor for the upper packed bed and the lower packed bed. However, the research results so far show that the formation of elemental sulfur is greater in the lower packed bed. Therefore, if the lower packed bed is washed more frequently than the upper packed bed, the upper packed bed Unnecessary detachment of microorganisms can be prevented and clogging of the lower packed bed can be suppressed. Therefore, the hydrogen sulfide removal performance of the biological desulfurization apparatus can be highly stabilized over a long period of time.

また、上記(1)の発明において、上段散気装置及び下段散気装置は、複数の空気の吐出口が形成された散気管を備え、該散気管は上段充填層及び下段充填層を支持する支持板のアングルに沿って配置され、且つ散気管の吐出口はアングルの反対側を向くように形成されている構成であることが好ましい。こうした構成にすることにより、散気管が水やガスの流路を妨げることが少なくなる。また、散気管の吐出口を下側となるように形成することにより、上段充填層(又は下段充填層)から落下した担体付着物が吐出口より進入して散気管が目詰まりすることを回避でき、洗浄効果を安定に維持できる。従って、生物脱硫装置の硫化水素除去性能を長期にわたって高く安定させることができる。   In the invention of (1), the upper stage diffuser and the lower stage diffuser include a diffuser pipe having a plurality of air discharge ports, and the diffuser pipe supports the upper packed bed and the lower packed bed. It is preferable that it is the structure which is arrange | positioned along the angle of a support plate, and is formed so that the discharge port of a diffuser may face the other side of an angle. By adopting such a configuration, the diffuser tube is less likely to obstruct the flow path of water or gas. In addition, by forming the discharge port of the air diffuser on the lower side, carrier deposits that have fallen from the upper packed bed (or the lower packed bed) are prevented from entering the discharge port and clogging the diffuser. The cleaning effect can be stably maintained. Therefore, the hydrogen sulfide removal performance of the biological desulfurization apparatus can be highly stabilized over a long period of time.

更に、上記(1)〜(3)の発明において、生物脱硫塔内を水で満たす際の水位を生物脱硫塔の外面の温度によって判定する構成であることが好ましい。即ち、生物脱硫塔において、水が満ちた部分の生物脱硫塔の外面は温度が水温に近く、水が満ちていない部分の生物脱硫塔の外面は室温に近くなるので、この境界線が水位と判断できる。従って、上記構成とすることにより、生物脱硫塔内の水位を容易に判断することができるので、洗浄作業をより容易に行うことができる。   Furthermore, in the above inventions (1) to (3), it is preferable that the water level when the inside of the biological desulfurization tower is filled with water is determined by the temperature of the outer surface of the biological desulfurization tower. That is, in the biodesulfurization tower, the temperature of the outer surface of the biodesulfurization tower in the part filled with water is close to the water temperature, and the outer surface of the biodesulfurization tower in the part not filled with water is close to room temperature. I can judge. Therefore, with the above configuration, the water level in the biological desulfurization tower can be easily determined, so that the cleaning operation can be performed more easily.

次に、本発明の実施形態に係る生物脱硫装置の具体的な例について図面を参照して説明する。なお、本実施形態は下記に述べることに限定されない。
(実施例1):請求項1,2に対応
図1を参照する。図中の符番1は、上部に開閉可能な蓋2を備えた生物脱硫塔である。この生物脱硫塔1内の上下には、上段充填層3、下段充填層4が夫々配置されている。上段充填層3は上段担体5aと該上段担体5aを支持する支持板6とから構成され、下段充填層4は下段担体5bと該下段担体5bを支持する支持板6とから構成されている。
Next, a specific example of the biological desulfurization apparatus according to the embodiment of the present invention will be described with reference to the drawings. Note that the present embodiment is not limited to the following description.
(Example 1): Corresponding to claims 1 and 2
Please refer to FIG. Reference numeral 1 in the figure is a biological desulfurization tower having a lid 2 that can be opened and closed at the top. An upper packed bed 3 and a lower packed bed 4 are arranged above and below the biodesulfurization tower 1, respectively. The upper packed bed 3 includes an upper carrier 5a and a support plate 6 that supports the upper carrier 5a, and the lower packed bed 4 includes a lower carrier 5b and a support plate 6 that supports the lower carrier 5b.

上段充填層3及び下段充填層4の下側には、上段散気装置7及び下段散気装置8が夫々配置されている。生物脱硫塔1内で上段充填層3の上部側にはシャワーノズル9が配置されており、このシャワーノズル9から水がポンプ10により噴射される。前記生物脱硫塔1の下部には、排水弁11を介装した処理水配管12が接続されている。上段散気装置7及び下段散気装置8には、ブロア13によりバルブ14a,14b,14cを介して空気が供給される。   Below the upper packed bed 3 and the lower packed bed 4, an upper diffuser 7 and a lower diffuser 8 are disposed, respectively. In the biological desulfurization tower 1, a shower nozzle 9 is arranged on the upper side of the upper packed bed 3, and water is injected from the shower nozzle 9 by a pump 10. A treated water pipe 12 having a drain valve 11 interposed is connected to the lower part of the biological desulfurization tower 1. Air is supplied to the upper air diffuser 7 and the lower air diffuser 8 through the valves 14a, 14b, and 14c by the blower 13.

生物脱硫塔1の底部には、生物脱硫塔1へバイオガスを導入するためのバルブ14eを介装したバイオガス流入管20が接続されている。バイオガス流入管20の途中には、バルブ14fを介装した配管18が接続され、コンプレッサー19によりバイオガス中の硫化水素の酸化分解に必要な空気がバイオガス流入管20に送られるようになっている。生物脱硫塔1の上部には、生物脱硫塔1内の処理ガスを排出するためのバルブ14dを介装した配管15が接続されている。バイオガス流入管20の入口側と配管15の出口側とは、バイパス弁16を介装したバイパス配管17により接続されている。生物脱硫装置の洗浄時には、バルブ14e及びバルブ14fを閉じ、バルブ16を開け、バイパス配管17を経由させることでバイオガスは生物脱硫装置をバイパスする。   Connected to the bottom of the biological desulfurization tower 1 is a biogas inflow pipe 20 having a valve 14 e for introducing biogas into the biological desulfurization tower 1. In the middle of the biogas inflow pipe 20, a pipe 18 having a valve 14 f is connected, and air necessary for oxidative decomposition of hydrogen sulfide in the biogas is sent to the biogas inflow pipe 20 by the compressor 19. ing. Connected to the upper part of the biological desulfurization tower 1 is a pipe 15 provided with a valve 14 d for discharging the processing gas in the biological desulfurization tower 1. The inlet side of the biogas inflow pipe 20 and the outlet side of the pipe 15 are connected by a bypass pipe 17 having a bypass valve 16 interposed therebetween. At the time of cleaning the biological desulfurization apparatus, the biogas bypasses the biological desulfurization apparatus by closing the valve 14e and the valve 14f, opening the valve 16, and passing through the bypass pipe 17.

こうした構成の生物脱硫装置では、蓋2を開け、排水弁11を閉じ、上段充填層3より上まで水によって満たした状態で、上段散気装置7に空気を供給して曝気を行うことで上段充填層3の洗浄を行う。また、その後、上段散気装置7を停止し、排水弁11を開け、水位を上段充填層3より下で且つ下段充填層4より上まで下げた状態で、下段散気装置8に空気を供給して曝気を行うことで下段充填層4の洗浄を行う。なお、前記水としては、例えば排水処理施設の二次処理水を利用する。   In the biological desulfurization apparatus having such a configuration, the upper stage is opened by supplying air to the upper stage air diffuser 7 in the state where the lid 2 is opened, the drain valve 11 is closed and the upper packed bed 3 is filled with water. The packed bed 3 is cleaned. After that, the upper air diffuser 7 is stopped, the drain valve 11 is opened, and air is supplied to the lower air diffuser 8 with the water level lowered below the upper packed bed 3 and above the lower packed bed 4. Then, the lower packed bed 4 is cleaned by aeration. In addition, as said water, the secondary treated water of a wastewater treatment facility is utilized, for example.

更に具体的に述べると、排水弁11を閉じ、ポンプ10により水を生物脱硫塔1に噴射することにより、生物脱硫塔1内は水で満ちていく。上段充填層3の下側に配置された上段散気装置7によって空気による曝気を行うと、気泡の浮力によって上段充填層3の担体が動き、担体の付着物が剥離する。ここで、曝気によって供給された空気は生物脱硫塔1の開口部より排出されるため、生物脱硫塔1の内圧が高まることはない。   More specifically, by closing the drain valve 11 and injecting water into the biological desulfurization tower 1 by the pump 10, the inside of the biological desulfurization tower 1 is filled with water. When aeration with air is performed by the upper air diffuser 7 arranged below the upper packed bed 3, the carrier of the upper packed bed 3 moves due to the buoyancy of the bubbles, and the deposits on the carrier are peeled off. Here, since the air supplied by aeration is discharged from the opening of the biological desulfurization tower 1, the internal pressure of the biological desulfurization tower 1 does not increase.

また、上段充填層3の洗浄を行うと、剥離した担体の付着物は下段充填層4に堆積するため、上段充填層3の洗浄を行った後に下段洗浄層4の洗浄を行うことで洗浄効果が高まる。さらに、弁の開閉の手間が少なく洗浄作業に要する時間が短くなる。
このように、実施例1に係る生物脱硫装置によれば、生物脱硫装置の上段充填層3及び下段充填層4の洗浄を最も少ない手間で行え、且つその洗浄効果を高くすることができる。
In addition, when the upper packing layer 3 is cleaned, the peeled carrier deposits are deposited on the lower packing layer 4, so that the cleaning effect is obtained by cleaning the lower cleaning layer 4 after cleaning the upper packing layer 3. Will increase. Furthermore, the time required for the cleaning operation is shortened with less time for opening and closing the valve.
Thus, according to the biological desulfurization apparatus which concerns on Example 1, cleaning of the upper stage packed bed 3 and the lower stage packed bed 4 of a biological desulfurization apparatus can be performed with the least effort, and the cleaning effect can be heightened.

なお、上記実施例1では、上段充填層3及び下段充填層4の洗浄の頻度について触れなかったが、例えば、次のような条件で洗浄を行うことにより、新たな効果を得ることができる。即ち、図1の生物脱硫装置において、蓋2を開け、排水弁11を閉じた後、シャワーノズル9より、下段充填層4より上まで水によって満たした状態で、下段散気装置8によって曝気を行うことで下段充填層4のみの洗浄を行い、下段充填層4の洗浄の頻度を上段充填層3の洗浄の頻度より短い間隔で実施することにより、生物脱硫装置の硫化水素の除去性能を長期にわたって高く安定させることができる。   In Example 1, the frequency of cleaning the upper packing layer 3 and the lower packing layer 4 was not mentioned. However, for example, a new effect can be obtained by cleaning under the following conditions. That is, in the biological desulfurization apparatus of FIG. 1, after the lid 2 is opened and the drain valve 11 is closed, aeration is performed by the lower air diffuser 8 in a state filled with water from the shower nozzle 9 to above the lower packed bed 4. In this way, only the lower packed bed 4 is cleaned, and the cleaning frequency of the lower packed bed 4 is performed at an interval shorter than the cleaning frequency of the upper packed bed 3, thereby improving the hydrogen sulfide removal performance of the biological desulfurization apparatus for a long time. Highly stable over time.

こうした効果が得られるのは次の理由による。即ち、脱硫反応により硫化水素は硫酸もしくは単体硫黄に変化する。硫酸は排水と共に排出されるが、単体硫黄は担体に付着して上段充填層3や下段充填層4の閉塞因子となる。これまでの研究結果より、単体硫黄の生成は下段充填層4に多いことが分かっているので、上述したように下段充填層4の洗浄を上段充填層3の洗浄よりも高頻度で実施することによって、上端充填層3の微生物の不必要な剥離を防止して下段充填層4の閉塞を抑制することができる。   This effect is obtained for the following reason. That is, hydrogen sulfide changes into sulfuric acid or elemental sulfur by the desulfurization reaction. The sulfuric acid is discharged together with the waste water, but the elemental sulfur adheres to the carrier and becomes a blocking factor for the upper packed bed 3 and the lower packed bed 4. From the research results so far, it is known that the formation of elemental sulfur is more in the lower packed bed 4, so that the lower packed bed 4 is cleaned more frequently than the upper packed bed 3 as described above. Thus, unnecessary detachment of microorganisms from the upper packed bed 3 can be prevented, and blockage of the lower packed bed 4 can be suppressed.

発明者らの実験によれば、下段充填層4の洗浄を10日間に1回、もしくは毎週1回実施し、そのうち月に1回の頻度で上段充填層3の洗浄も行うようにすることが生物脱硫装置の硫化水素除去性能を安定させるのに適切であった。これは下段充填層4に付着した単体硫黄量が上段充填層3の4〜5倍であったことと合わせて考えると単体硫黄の生成量に応じて適切な頻度であったと判断される。さらに洗浄において、空気を供給して曝気を行う時間は、1分を越えると過剰であり、時間が1分30秒のとき、硫化水素除去性能は低下した。時間は30秒で十分であった。即ち、充填層から単体硫黄を剥離せしめるには、担体のわずかな遊動で十分だと考えられた。なお、下段充填層4と上段充填層3との洗浄の条件が上記した頻度、時間に限定されないのは勿論のことである。   According to the experiments by the inventors, the lower packed bed 4 is cleaned once every 10 days or once every week, and the upper packed bed 3 is also cleaned once a month. It was suitable to stabilize the hydrogen sulfide removal performance of biological desulfurization equipment. Considering that the amount of simple sulfur adhering to the lower packed bed 4 is 4 to 5 times that of the upper packed bed 3, it is determined that the frequency was appropriate depending on the amount of generated single sulfur. Further, in the cleaning, the time for supplying air and performing aeration is excessive when it exceeds 1 minute, and when the time is 1 minute 30 seconds, the hydrogen sulfide removing performance is lowered. A time of 30 seconds was sufficient. That is, it was considered that a slight movement of the carrier was sufficient to peel off the elemental sulfur from the packed bed. It goes without saying that the cleaning conditions for the lower packed bed 4 and the upper packed bed 3 are not limited to the frequency and time described above.

(実施例2):請求項3に対応
図2(A),(B),(C)を参照する。ここで、図2(A)は生物脱硫装置の一構成である上段充填層の支持板の概略的な平面図、図2(B)は上段充填層の下側に配置される上段散気装置の一構成である配管とバルブ,ブロワとの関係を示す概略的な平面図、図2(C)は図2(B)の散気管を部分的に拡大した裏面図である。但し、図1と同部材は同符番を付して説明を省略する。また、下段充填層も上段充填層と同様な構成になっているので、説明を省略する。
(Example 2): Corresponding to claim 3
Reference is made to FIGS. 2A, 2B, and 2C. Here, FIG. 2 (A) is a schematic plan view of a support plate for the upper packed bed, which is one configuration of the biological desulfurization apparatus, and FIG. 2 (B) is an upper diffuser disposed below the upper packed bed. 2 is a schematic plan view showing the relationship between a pipe, a valve, and a blower, which is one configuration, and FIG. 2 (C) is a back view partially enlarged of the air diffuser of FIG. 2 (B). However, the same members as those in FIG. Moreover, since the lower packed bed has the same configuration as the upper packed bed, the description thereof is omitted.

支持板6は、縦横に略均等に配置されたアングル21と、これらのアングル21の上部に配置されたパンチングメタル22とから構成されている。支持板6の下部には、上段散気装置7を構成する複数の散気管23が一方向(図2(A)の上下方向)に沿うアングル21に沿って配置されている。散気管23には、アングル21の反対方向を向くように空気の吐出口23aが形成されている。各散気管23には、バルブ24を夫々介装した配管25が接続されている。これらの配管25は、バルブ26を介装した配管27によりブロワ13に接続されている。   The support plate 6 is composed of angles 21 that are arranged substantially evenly in the vertical and horizontal directions, and a punching metal 22 that is arranged on top of these angles 21. In the lower part of the support plate 6, a plurality of air diffusers 23 constituting the upper air diffuser 7 are arranged along an angle 21 along one direction (the vertical direction in FIG. 2A). An air discharge port 23 a is formed in the air diffuser 23 so as to face the direction opposite to the angle 21. Each diffuser pipe 23 is connected to a pipe 25 having a valve 24 interposed therebetween. These pipes 25 are connected to the blower 13 by a pipe 27 having a valve 26 interposed therebetween.

上記実施例2によれば、散気管23を支持板6のアングル21に沿って配置した構成にすることにより、散気管23が水やガスの流路を妨げることが少なくなる。また、散気管23の吐出口23aを下側となるように形成することにより、上段充填層3(又は下段充填層4)から落下した担体付着物が吐出口23aより進入して散気管23が目詰まりすることを回避でき、洗浄効果を安定に維持できる。従って、生物脱硫装置の硫化水素除去性能を長期にわたって高く安定させることができる。   According to the second embodiment, the configuration in which the air diffuser 23 is disposed along the angle 21 of the support plate 6 makes it less likely that the air diffuser 23 obstructs the flow path of water or gas. Further, by forming the discharge port 23a of the diffuser tube 23 to be on the lower side, the carrier deposits that have fallen from the upper packed bed 3 (or the lower packed bed 4) enter from the discharge port 23a and the diffused tube 23 is formed. Clogging can be avoided and the cleaning effect can be maintained stably. Therefore, the hydrogen sulfide removal performance of the biological desulfurization apparatus can be highly stabilized over a long period of time.

(実施例3):請求項4に対応
図1を参照する。本実施例3では、前記蓋2を開け、前記排水弁11を閉じ、前記上段充填層3(又は下段充填層4)の支持板6が浸るまで水によって満たし、上段散気装置7(又は下段散気装置8)によって曝気を行うことで上段充填層3(又は下段充填層4)の支持板6の洗浄を行う構成になっている。
(Example 3): Corresponding to claim 4
Please refer to FIG. In the third embodiment, the lid 2 is opened, the drain valve 11 is closed, and the upper stage packed bed 3 (or the lower stage packed bed 4) is filled with water until the support plate 6 is immersed, and the upper stage diffuser 7 (or the lower stage is installed). The support plate 6 of the upper packed bed 3 (or the lower packed bed 4) is cleaned by aeration with the diffuser 8).

実施例3によれば、上段充填層3(又は下段充填層4)の支持板6が浸るまで水を満たすことで、支持板6の洗浄を行うことができる。しかも、ほとんど全ての担体は水に浸っていないので、担体の付着物が水によって剥離することが極めて少ない。従って、支持板6のみの洗浄を長時間にわたって行うことができるので、生成物による支持板6の閉塞が防止でき、生物脱硫装置の硫化水素除去性能を長期にわたって高く安定させることができる。   According to Example 3, the support plate 6 can be cleaned by filling the water until the support plate 6 of the upper packed bed 3 (or the lower packed bed 4) is immersed. In addition, since almost all of the carrier is not immersed in water, deposits on the carrier are very rarely peeled off by water. Accordingly, since only the support plate 6 can be washed for a long time, the support plate 6 can be prevented from being blocked by the product, and the hydrogen sulfide removal performance of the biological desulfurization apparatus can be highly stabilized over a long period of time.

(実施例4):請求項5に対応
図3を参照する。但し、図1と同部材は同符番を付して説明を省略する。
図中の符番31は、上段充填層3及び下段充填層4を経由して生物脱硫塔1の底部まで滴下して滞留する底部滞留水32の一部を上段充填層3の上部より散布する循環装置である。循環装置31は、生物脱硫塔1の上部と下部に接続された配管33と、この配管33に介装されたバルブ34,循環水槽35及び循環ポンプ36と、配管33に接続された液散布管37とから構成されている。
こうした構成の生物脱硫装置においては、上部充填層3の微生物が洗浄によって過剰に剥離した場合、循環装置31による底部滞留水32の循環とシャワーノズル9による水の散布とを併用することにより上段充填層3の微生物量を回復させる構成となっている。
(Example 4): Corresponding to claim 5
Please refer to FIG. However, the same members as those in FIG.
The reference numeral 31 in the figure is a part of the bottom accumulated water 32 that drops and stays at the bottom of the biological desulfurization tower 1 via the upper packed bed 3 and the lower packed bed 4 from the upper part of the upper packed bed 3. It is a circulation device. The circulation device 31 includes a pipe 33 connected to the upper and lower parts of the biological desulfurization tower 1, a valve 34 interposed in the pipe 33, a circulating water tank 35 and a circulation pump 36, and a liquid spray pipe connected to the pipe 33. 37.
In the biological desulfurization apparatus having such a configuration, when microorganisms in the upper packed bed 3 are excessively separated by washing, upper stage filling is performed by using both circulation of the bottom accumulated water 32 by the circulation apparatus 31 and water spraying by the shower nozzle 9. The layer 3 is configured to recover the amount of microorganisms.

図4の生物脱硫装置において、上段充填層3から剥離した微生物は下段充填層4に落下するので、下段充填層4は上段充填層3より微生物が供給される。一方、上段充填層3にはどこからも微生物の供給がないため、微生物が増殖するまでに下段充填層4より時間を要する。しかして、実施例4では、上部充填層3の微生物が洗浄によって過剰に剥離した場合、循環装置31による底部滞留水32の循環とシャワーノズル9による水の散布とを併用することにより上段充填層3の微生物量を回復させる構成であるので、循環装置31によって底部滞留水32を上段充填層3に散布することで、下段充填層4から剥離した微生物を上段充填層3へ供給でき、上段充填層3の微生物量を短時間で増加させることができる。従って、過洗浄による担体からの微生物の剥離による生物脱硫装置の硫化水素除去性能の低下を短期で回復することができる。   In the biological desulfurization apparatus of FIG. 4, the microorganisms detached from the upper packed bed 3 fall into the lower packed bed 4, so that the lower packed bed 4 is supplied with microorganisms from the upper packed bed 3. On the other hand, since the microorganisms are not supplied from anywhere in the upper packed bed 3, it takes more time than the lower packed bed 4 until the microorganisms grow. Thus, in Example 4, when the microorganisms in the upper packed bed 3 are excessively separated by washing, the upper packed bed is obtained by using both the circulation of the bottom accumulated water 32 by the circulation device 31 and the spraying of the water by the shower nozzle 9. 3 is recovered so that the microorganisms separated from the lower packed bed 4 can be supplied to the upper packed bed 3 by spraying the bottom stagnant water 32 on the upper packed bed 3 by the circulation device 31, and the upper packed The amount of microorganisms in the layer 3 can be increased in a short time. Accordingly, it is possible to recover in a short time the deterioration of the hydrogen sulfide removal performance of the biological desulfurization apparatus due to the detachment of microorganisms from the carrier due to overwashing.

なお、循環装置31による底部滞留水32の循環とシャワーノズル9による水の散布とを併用する場合は、水の散布量を少なくすることが望ましい。これは、上段充填層3及び下段充填層4を通過する液の量が過大となり、微生物の剥離する量が増加することを防ぐためで、少なくとも循環させる底部滞留水32の水量分は差し引くとよい。   In addition, when using together circulation of the bottom part retention water 32 by the circulation apparatus 31, and spraying of the water by the shower nozzle 9, it is desirable to reduce the amount of spraying of water. This is to prevent the amount of the liquid passing through the upper packed bed 3 and the lower packed bed 4 from becoming excessive and increase the amount of microorganisms to be peeled off. At least the amount of the bottom retained water 32 to be circulated should be subtracted. .

(実施例5):請求項6に対応
図4(A),(B)を参照する。ここで、図4(A)は実施例5の生物脱硫装置の概略的な説明図であり、図4(B)は同生物脱硫装置の生物脱硫塔内の水位の塔高さと塔外面温度との関係を示す特性図である。但し、図1と同部材は同符番を付して説明を省略する。 実施例5の生物脱硫装置は、生物脱硫塔1内を水38で満たす際の水位を生物脱硫塔1の外面の温度によって判定する構成としたことを特徴とする。ここで、温度の測定には温度計を用いることができるが、赤外線サーモグラフィ等を用いるとより簡単に水位が判断できる。こうした構成の装置では、水38が満ちた部分の生物脱硫塔1の外面は温度が水温に近く、水が満ちていない部分の生物脱硫塔1の外面は室温に近くなる(図4(B)参照)。従って、この境界線が水位と判断できる。このように、実施例5によれば、生物脱硫塔1内の水位を容易に判断することができるので、洗浄作業をより容易に行うことができる。
(Example 5): Corresponding to Claim 6
Reference is made to FIGS. Here, FIG. 4 (A) is a schematic explanatory diagram of the biological desulfurization apparatus of Example 5, and FIG. 4 (B) shows the tower height of the water level and the tower outer surface temperature in the biological desulfurization tower of the biological desulfurization apparatus. It is a characteristic view which shows the relationship. However, the same members as those in FIG. The biodesulfurization apparatus of Example 5 is characterized in that the water level when the biodesulfurization tower 1 is filled with water 38 is determined by the temperature of the outer surface of the biodesulfurization tower 1. Here, a thermometer can be used for temperature measurement, but the water level can be more easily determined by using infrared thermography or the like. In the apparatus having such a configuration, the temperature of the outer surface of the biological desulfurization tower 1 filled with water 38 is close to the water temperature, and the outer surface of the biological desulfurization tower 1 filled with water is close to room temperature (FIG. 4B). reference). Therefore, this boundary line can be determined as the water level. Thus, according to Example 5, since the water level in the biological desulfurization tower 1 can be easily determined, the cleaning operation can be performed more easily.

(実施例6):請求項7に対応
図5を参照する。但し、図1と同部材は同符番を付して説明を省略する。
図中の符番41は高圧洗浄装置の高圧洗浄ノズルであり、上段充填層3及び下段充填層4の下側に夫々配置されている。図5の生物脱硫装置では、高圧洗浄装置の高圧洗浄ノズル41に水を供給することにより、上段充填層3及び下段充填層4の洗浄を行う構成になっている。
Example 6: Corresponding to Claim 7
Please refer to FIG. However, the same members as those in FIG.
Reference numeral 41 in the figure denotes a high-pressure cleaning nozzle of the high-pressure cleaning device, which is disposed below the upper packed bed 3 and the lower packed bed 4, respectively. The biological desulfurization apparatus of FIG. 5 is configured to clean the upper packed bed 3 and the lower packed bed 4 by supplying water to the high pressure cleaning nozzle 41 of the high pressure cleaning apparatus.

実施例6によれば、上段充填層3及び下段充填層4の支持板6の下側から加圧水を噴射することによって、支持板6の付着物を剥離することができる。また、水圧によって担体を動かすことで、担体の付着物を剥離し易くすることができる。その結果、生物脱硫塔1内に水を張る必要がなく、支持板6の洗浄を短時間で行うことができ、洗浄による生物脱硫装置の停止時間を短くできる。このように、実施例6によれば、生物脱硫装置の上段充填層3及び下段充填層4の洗浄を短時間で行うことができ、生物脱硫装置の硫化水素除去性能を長期にわたって高く安定させることができる。   According to Example 6, the deposits on the support plate 6 can be peeled off by spraying pressurized water from below the support plate 6 of the upper packed bed 3 and the lower packed bed 4. Further, by moving the carrier by water pressure, it is possible to easily peel off the deposit on the carrier. As a result, it is not necessary to fill the biological desulfurization tower 1 with water, the support plate 6 can be cleaned in a short time, and the stop time of the biological desulfurization apparatus due to the cleaning can be shortened. Thus, according to Example 6, the upper packed bed 3 and the lower packed bed 4 of the biological desulfurization apparatus can be cleaned in a short time, and the hydrogen sulfide removal performance of the biological desulfurization apparatus can be highly stabilized over a long period of time. Can do.

なお、本発明は、上記実施形態そのままに限定されるものではなく、実施段階ではその要旨を逸脱しない範囲で構成要素を変形して具体化できる。また、上記実施形態に開示されている複数の構成要素の適宜な組み合せにより種々の発明を形成できる。例えば、実施形態に示される全構成要素から幾つかの構成要素を削除してもよい。更に、異なる実施形態に亘る構成要素を適宜組み合せてもよい。具体的には、上記実施例では、生物脱硫塔の上部に開閉可能な蓋を設けた場合について述べたが、これに限らず、生物脱硫塔の上部にバルブを設けてもよい。   Note that the present invention is not limited to the above-described embodiment as it is, and can be embodied by modifying the constituent elements without departing from the scope of the invention in the implementation stage. Further, various inventions can be formed by appropriately combining a plurality of constituent elements disclosed in the embodiment. For example, some components may be deleted from all the components shown in the embodiment. Furthermore, you may combine suitably the component covering different embodiment. Specifically, in the above-described embodiment, the case where an openable / closable lid is provided at the top of the biological desulfurization tower is described. However, the present invention is not limited thereto, and a valve may be provided at the top of the biological desulfurization tower.

本発明の実施例1に係る生物脱硫装置の概略的な説明図。BRIEF DESCRIPTION OF THE DRAWINGS Schematic explanatory drawing of the biological desulfurization apparatus which concerns on Example 1 of this invention. 本発明の実施例2に係る生物脱硫装置の生物脱硫装置の一構成である上段充填層等の説明図。Explanatory drawing of the upper stage packed bed etc. which are one structure of the biodesulfurization apparatus of the biodesulfurization apparatus which concerns on Example 2 of this invention. 本発明の実施例4に係る生物脱硫装置の概略的な全体図。FIG. 6 is a schematic overall view of a biological desulfurization apparatus according to Embodiment 4 of the present invention. 本発明の実施例5に係る生物脱硫装置の説明図。Explanatory drawing of the biological desulfurization apparatus which concerns on Example 5 of this invention. 本発明の実施例6に係る生物脱硫装置の概略的な説明図。Schematic explanatory drawing of the biological desulfurization apparatus which concerns on Example 6 of this invention.

符号の説明Explanation of symbols

1…生物反応槽、2…上部蓋、3…上段充填層、4…下段充填層、5a…上段担体、5b…下段担体、6…支持板、7…上段散気装置、8…下段散気装置、9,37…シャワーノズル、10…ポンプ、11…排水弁、12…処理水配管、14a〜14f,34…バルブ、16…バイパス弁、17…バイパス管、19…コンプレッサー、20…バイオガス流入管、21…アングル、22…パンチグメタル、23…散気管、35…循環水槽、36…循環ポンプ、38…底部滞留水、41…高圧洗浄ノズル。   DESCRIPTION OF SYMBOLS 1 ... Biological reaction tank, 2 ... Upper lid, 3 ... Upper stage packed bed, 4 ... Lower stage packed bed, 5a ... Upper stage carrier, 5b ... Lower stage carrier, 6 ... Support plate, 7 ... Upper stage diffuser, 8 ... Lower stage diffuser Apparatus, 9, 37 ... Shower nozzle, 10 ... Pump, 11 ... Drain valve, 12 ... Treated water piping, 14a-14f, 34 ... Valve, 16 ... Bypass valve, 17 ... Bypass pipe, 19 ... Compressor, 20 ... Biogas Inflow pipe, 21 ... angle, 22 ... punch metal, 23 ... diffuser pipe, 35 ... circulating water tank, 36 ... circulating pump, 38 ... bottom accumulated water, 41 ... high pressure washing nozzle.

Claims (7)

上部に開閉可能な蓋もしくはバルブを備えた生物脱硫塔と、この生物脱硫塔内の上下に夫々配置され,担体及び該担体を支持する支持板からなる上段充填層及び下段充填層と、これらの上段充填層及び下段充填層の下側に夫々配置された上段散気装置及び下段散気装置と、前記生物脱硫塔の下部に接続された,排水弁を介装した処理水配管とを具備した生物脱硫装置であって、
前記蓋もしくはバルブを開け、前記排水弁を閉じ、前記上段充填層より上まで水によって満たした状態で、前記上段散気装置に空気を供給して曝気を行うことで前記上段充填層の洗浄を行い、
その後、前記上段散気装置を停止し、前記排水弁を開け、水位を前記上段充填層より下で且つ前記下段充填層より上まで下げた状態で、前記下段散気装置に空気を供給して曝気を行うことで前記下段充填層の洗浄を行う構成であることを特徴とする生物脱硫装置。
A biological desulfurization tower having a lid or a valve that can be opened and closed at the top; an upper packed bed and a lower packed bed, each of which is arranged above and below the biological desulfurization tower and includes a support and a support plate that supports the support; The upper stage aeration apparatus and the lower stage aeration apparatus respectively disposed on the lower side of the upper stage packed bed and the lower stage packed bed, and a treated water pipe connected to the lower part of the biological desulfurization tower and provided with a drain valve. A biological desulfurization device,
In the state where the lid or valve is opened, the drain valve is closed and the upper filling layer is filled with water, the upper filling layer is cleaned by supplying air to the upper aeration device and performing aeration. Done
Thereafter, the upper air diffuser is stopped, the drain valve is opened, and air is supplied to the lower air diffuser in a state where the water level is lowered below the upper packed bed and above the lower packed bed. A biological desulfurization apparatus characterized in that the lower packed bed is washed by aeration.
請求項1記載の上段充填層及び下段充填層を洗浄する手段と、
前記蓋若しくはバルブを開け、前記排水弁を閉じ、前記下段充填層より上まで水によって満たした状態で、前記下段散気装置によって曝気を行うことで下段充填層の洗浄を行う、下段充填層の洗浄手段を有し、
下段充填層のみの洗浄の頻度を、上段充填層の洗浄の頻度より短い間隔で実施する構成であることを特徴とする生物脱硫装置。
Means for cleaning the upper packed bed and the lower packed bed according to claim 1;
Opening the lid or valve, closing the drain valve, and cleaning the lower packed bed by aeration with the lower diffuser in a state filled with water above the lower packed bed. Having cleaning means,
A biological desulfurization apparatus characterized in that the frequency of cleaning only the lower packed bed is performed at an interval shorter than the frequency of cleaning the upper packed bed.
前記上段散気装置及び下段散気装置は、複数の空気の吐出口が形成された散気管を備え、該散気管は前記上段充填層及び下段充填層を支持する支持板のアングルに沿って配置され、且つ散気管の吐出口はアングルの反対側を向くように形成されている構成であることを特徴とする請求項1若しくは2記載の生物脱硫装置。 The upper-stage diffuser and the lower-stage diffuser include a diffuser pipe having a plurality of air discharge ports, and the diffuser pipe is disposed along an angle of a support plate that supports the upper-stage packed bed and the lower-stage packed bed. The biodesulfurization apparatus according to claim 1 or 2, wherein the discharge port of the air diffuser is configured to face the opposite side of the angle. 上部に開閉可能な蓋もしくはバルブを備えた生物脱硫塔と、この生物脱硫塔内の上下に夫々配置され,担体及び該担体を支持する支持板からなる上段充填層及び下段充填層と、これらの上段充填層及び下段充填層の下側に夫々配置された上段散気装置及び下段散気装置と、前記生物脱硫塔の下部に接続された,排水弁を介装した処理水配管とを具備した生物脱硫装置であって、
前記蓋もしくはバルブを開け、前記排水弁を閉じ、前記上段充填層又は下段充填層の支持板が浸るまで水によって満たし、上段散気装置又は下段散気装置によって曝気を行うことで上段充填層又は下段充填層の支持板の洗浄を行う構成であることを特徴とする生物脱硫装置。
A biological desulfurization tower having a lid or a valve that can be opened and closed at the top; an upper packed bed and a lower packed bed, each of which is arranged above and below the biological desulfurization tower and includes a support and a support plate that supports the support; The upper stage aeration apparatus and the lower stage aeration apparatus respectively disposed on the lower side of the upper stage packed bed and the lower stage packed bed, and a treated water pipe connected to the lower part of the biological desulfurization tower and provided with a drain valve. A biological desulfurization device,
Open the lid or valve, close the drain valve, fill with water until the support plate of the upper packed bed or the lower packed bed is immersed, and perform aeration with the upper diffuser or the lower diffuser to perform the upper packed bed or A biological desulfurization apparatus characterized in that the support plate of the lower packed bed is washed.
生物脱硫塔と、この生物脱硫塔内の上下に配置された上段充填層及び下段充填層と、前記生物脱硫塔内の上部に配置された,水の散布を行うシャワーノズルと、上段充填層及び下段充填層を経由して生物脱硫塔の底部まで滴下して滞留する底部滞留水の一部を上段充填層の上部より散布する循環装置と、前記生物脱硫塔の下部に接続された,排水弁を介装した処理水配管とを具備した生物脱硫装置であって、
前記上部充填層の微生物が洗浄によって過剰に剥離した場合、前記循環装置による底部滞留水の循環と前記シャワーノズルによる水の散布とを併用することにより上段充填層の微生物量を回復する構成であることを特徴とする生物脱硫装置。
A biological desulfurization tower, an upper packed bed and a lower packed bed disposed above and below in the biological desulfurized tower, a shower nozzle for spraying water disposed at an upper portion in the biological desulfurized tower, an upper packed bed, and A circulation device for spraying a part of the bottom retained water that drops and stays to the bottom of the biological desulfurization tower via the lower packed bed from the upper part of the upper packed bed, and a drain valve connected to the lower part of the biological desulfurization tower A biological desulfurization apparatus comprising a treated water pipe intervening,
When microorganisms in the upper packed bed are excessively separated by washing, the amount of microorganisms in the upper packed bed is recovered by using both the circulation of the bottom accumulated water by the circulation device and the spraying of water by the shower nozzle. A biological desulfurization apparatus characterized by that.
前記生物脱硫塔内を水で満たす際の水位を生物脱硫塔の外面の温度によって判定する構成であることを特徴とする請求項1乃至5いずれか一記載の生物脱硫塔。 The biodesulfurization tower according to any one of claims 1 to 5, wherein the biodesulfurization tower is configured to determine a water level when the biodesulfurization tower is filled with water based on a temperature of an outer surface of the biodesulfurization tower. 上部に開閉可能な蓋もしくはバルブを備えた生物脱硫塔と、この生物脱硫塔内の上下に夫々配置され,担体及び該担体を支持する支持板からなる上段充填層及び下段充填層と、これらの上段充填層及び下段充填層の下側に夫々配置された,高圧洗浄ノズルを有した高圧洗浄装置と、前記生物脱硫塔の下部に接続された,排水弁を介装した処理水配管とを具備した生物脱硫装置であって、
前記高圧洗浄装置の高圧洗浄ノズルに水を供給することにより前記上段充填層及び下段充填層の洗浄を行う構成であることを特徴とする生物脱硫装置。
A biological desulfurization tower having a lid or a valve that can be opened and closed at the top; an upper packed bed and a lower packed bed, each of which is arranged above and below the biological desulfurization tower and includes a support and a support plate that supports the support; A high-pressure washing apparatus having a high-pressure washing nozzle, which is arranged below the upper packed bed and the lower packed bed, respectively, and a treated water pipe connected to the lower part of the biological desulfurization tower and provided with a drain valve A biological desulfurization device,
A biodesulfurization apparatus characterized in that the upper packed bed and the lower packed bed are cleaned by supplying water to the high pressure cleaning nozzle of the high pressure cleaning apparatus.
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JP2015003291A (en) * 2013-06-20 2015-01-08 株式会社東芝 Biological desulfurization method, and biological desulfurization apparatus

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