JP2022160854A - Deodorization apparatus and deodorization method - Google Patents

Deodorization apparatus and deodorization method Download PDF

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JP2022160854A
JP2022160854A JP2021065322A JP2021065322A JP2022160854A JP 2022160854 A JP2022160854 A JP 2022160854A JP 2021065322 A JP2021065322 A JP 2021065322A JP 2021065322 A JP2021065322 A JP 2021065322A JP 2022160854 A JP2022160854 A JP 2022160854A
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water tank
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敏晃 乾
Toshiaki Inui
祐治 小関
Yuji Koseki
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Seeplan Co Ltd
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Abstract

To provide a deodorization apparatus having high deodorization performance and being compactified and to provide a deodorization method.SOLUTION: In a deodorization apparatus having a plurality of packed beds, a plurality of water storage tanks cultivating microorganisms and a sprinkler mechanism, fillers carried with microorganisms are filled in the packed beds connected so as to flow a malodorous gas; the water storage tanks are connected so as to flow water; the sprinkler mechanism is a mechanism sprinkling water in at least one water storage tank at a downstream from an uppermost stream water storage tank to the packed beds; and the packed bed and the water storage tank are connected so that sprinkled water passing the packed bed is introduced into an upstream water storage tank from the water storage tank becoming a sprinkling water supply source.SELECTED DRAWING: Figure 1

Description

本発明は、微生物を利用した脱臭装置及び脱臭方法に関する。 TECHNICAL FIELD The present invention relates to a deodorizing device and a deodorizing method using microorganisms.

養豚場等の畜産施設からは臭気が発生し、その発生源は主に豚舎等の畜舎と糞尿のコンポストである。これらから発生する臭気は不快で強烈な臭気(悪臭)であり、近隣からの苦情の原因となっている。そのため、臭気を除くために、バブリングやスクラバー方式で臭気ガスを水に溶解させる水洗法、臭気成分を薬液に吸着させ化学的に中和する薬液処理法、オガクズやモミガラに臭気成分を吸着させる方法、オゾンの酸化力で臭気成分を分解するオゾン脱臭法等の脱臭方法が使用されている。また、微生物による臭気成分の分解作用を利用した生物脱臭方法として、土壌を用いる方法である土壌脱臭法、ロックウールを主体とした材料に有機物や微生物源を混合調整した脱臭材料を使用する方法、微生物を保持できる充填材(担体)を塔内に充填し、充填層内に臭気ガスを通過させて、微生物に臭気成分を分解させる充填塔式生物脱臭法等が使用されている。この中でも、充填塔式生物脱臭法は、維持管理が容易であり、充填材に担持させる微生物の密度を高くできることが期待されるため、いくつかの方法が提案されている。例えば、特許文献1に記載の方法は、脱臭塔内に充填材を充填し、悪臭ガスを脱臭塔内に導入して充填層中を通過させ、その際悪臭ガス中に含まれる悪臭成分を微生物により分解する方法であり、さらに、貯水槽から汲み上げた水を充填層に散水し、充填層を通過してきた水を再度貯水槽に戻して散水用の水を循環させている。しかしながら、微生物の分解能力は充填材への担持後、時間とともに低下していくため、脱臭性能を維持することは難しい。特許文献1に記載の方法では、貯水槽のORP、pHを管理し、貯水槽に栄養成分を添加することにより、脱臭性能の低下を防止しようとしているが、十分ではなかった。また、脱臭性能を維持するためには、装置をコンパクト化することも難しかった。 Odor is generated from livestock facilities such as pig farms, and the source of the odor is mainly livestock barns such as piggeries and manure compost. The odors emitted from these are unpleasant and strong odors (bad odors), and are the cause of complaints from neighbors. Therefore, in order to remove the odor, there is a water washing method in which odorous gases are dissolved in water using a bubbling or scrubber method, a chemical solution treatment method in which odorous components are adsorbed in a chemical solution and chemically neutralized, and a method in which sawdust and rice husks adsorb odorous components. , an ozone deodorizing method in which odorous components are decomposed by the oxidizing power of ozone. Biological deodorizing methods utilizing the decomposition of malodorous components by microorganisms include a soil deodorizing method using soil, a method using a deodorizing material in which organic matter and microbial sources are mixed with a material mainly composed of rock wool, A packed tower type biological deodorization method or the like is used in which a column is filled with a packing material (carrier) capable of retaining microorganisms, and odorous gases are passed through the packed bed to cause the microorganisms to decompose the odorous components. Among these, since the packed tower type biological deodorization method is easy to maintain and is expected to increase the density of microorganisms carried on the filler, several methods have been proposed. For example, in the method described in Patent Document 1, the deodorizing tower is filled with a packing material, the malodorous gas is introduced into the deodorizing tower and passed through the packed bed, and at that time the malodorous components contained in the malodorous gas are removed by microorganisms. Furthermore, the water pumped up from the water storage tank is sprinkled on the packed bed, and the water that has passed through the packed bed is returned to the water storage tank again to circulate the water for watering. However, it is difficult to maintain the deodorizing performance because the decomposition ability of microorganisms decreases with time after being supported on the filler. In the method described in Patent Literature 1, the ORP and pH of the water tank are controlled, and nutrients are added to the water tank to prevent deterioration of the deodorizing performance, but this was not sufficient. Moreover, in order to maintain the deodorizing performance, it has been difficult to make the device compact.

特開平6-99021号公報JP-A-6-99021

本発明は、脱臭性能が高い脱臭装置及び脱臭方法を提供することを課題とする。また、コンパクト化できる脱臭装置及び脱臭方法を提供することを課題とする。 An object of the present invention is to provide a deodorizing device and a deodorizing method with high deodorizing performance. Another object of the present invention is to provide a compact deodorizing device and a deodorizing method.

本発明者らは、脱臭性能に優れ、コンパクト化の可能な脱臭装置及び脱臭方法の検討を開始した。従来、脱臭のために微生物を含有する充填層を使用する方法が提案され、この充填層には臭気成分であるアンモニアを溶解させるために水が散水されていた。散水され充填層を通過した水には微生物が含まれているため、この水を貯水槽に溜め貯水槽のpHを調整し、栄養成分を添加して貯水槽に溜めた水を再度散水することが提案されている。これは、微生物の活性を維持しながら充填層と貯水槽の間で水を循環させようとする試みである。しかしながら、十分な効果は得られていない。本発明者らは、貯水槽における微生物の活性を維持するのではなく、むしろ積極的に微生物を培養し増殖させ、このような微生物を含む水を充填層に散水すれば、脱臭効果を向上させられるのではないかと考え検討を進めたところ、貯水槽を複数使用して微生物を含んだ水を貯水槽の間でゆっくり移動させると、微生物の培養効果に優れ微生物を増殖できることを見いだした。さらに、充填層、充填層を通過した水が溜まる貯水槽及び散水する水を供給する貯水槽との関係を特定の関係とすると微生物の培養効果が更に優れることを見いだした。また、充填層における脱臭効果が非常に高まることから、装置をコンパクト化できることを見いだした。さらに、このような脱臭装置及び脱臭方法は、充填層における脱臭効果が非常に高まることにより充填材の使用量を減らすことができ、コンパクト化により装置の製造に要する費用、設置工事費、ランニングコスト、管理の手間、また設置スペースを減らすことができるので、脱臭処理を低コスト化できるものであった。本発明は、こうして完成されたものである。 The present inventors have started to study a deodorizing device and a deodorizing method that are excellent in deodorizing performance and can be made compact. Conventionally, a method of using a packed bed containing microorganisms for deodorization has been proposed, and water has been sprinkled on this packed bed in order to dissolve ammonia, which is an odor component. Since the water that has been sprayed and passed through the packed bed contains microorganisms, this water is stored in a water storage tank, the pH of the water storage tank is adjusted, nutrients are added, and the water stored in the water storage tank is sprinkled again. is proposed. This is an attempt to circulate water between the packed bed and the reservoir while maintaining microbial activity. However, sufficient effects have not been obtained. The present inventors have found that, rather than maintaining the activity of microorganisms in a water tank, the deodorizing effect can be improved by actively culturing and growing microorganisms and sprinkling water containing such microorganisms on a packed bed. As a result, it was found that using multiple water tanks and slowly moving the water containing microorganisms between the water tanks has an excellent culturing effect for microorganisms and enables the growth of microorganisms. Further, the inventors have found that the effect of culturing microorganisms is further improved when the relationship between the packed bed, the water tank in which the water that has passed through the packed bed is stored, and the water tank that supplies the water to be sprayed is in a specific relationship. In addition, it was found that the apparatus can be made compact because the deodorizing effect in the packed bed is greatly enhanced. Furthermore, such a deodorizing device and deodorizing method can reduce the amount of filler used because the deodorizing effect in the packed bed is greatly enhanced, and the cost required for manufacturing the device, installation work cost, and running cost due to compactness. , the labor of management and the installation space can be reduced, so that the cost of deodorizing treatment can be reduced. The present invention is thus completed.

すなわち、本発明は以下に示す事項により特定されるものである。
(1)臭気ガスを通過させ脱臭するための複数の充填層、微生物を培養するための複数の貯水槽及び前記充填層に前記貯水槽の水を散水するための散水機構を備えた脱臭装置であって、
前記充填層には、微生物を担持した充填材が充填され、
前記充填層は、前記臭気ガスが導入される最上流の充填層から前記臭気ガスが排出される最下流の充填層まで、前記臭気ガスが流れるように連結され、
前記貯水槽は、前記脱臭装置の外部より前記水が供給される最上流の貯水槽から最下流の貯水槽まで、前記水が流れるように連結され、
前記散水機構は、前記最上流の貯水槽より下流の少なくとも1つの貯水槽の水を前記充填層に散水する機構であり、
散水する水の供給元となる貯水槽より上流の貯水槽に、充填層を通過した散水された水が導入されるように、前記充填層と前記貯水槽が連結されている脱臭装置。
(2)散水する水の供給元となる貯水槽及び前記貯水槽より上流の貯水槽は、隣り合う貯水槽の下流側の貯水槽が、上流側の貯水槽に連結されている充填層よりも下流の充填層に連結されていることを特徴とする上記(1)の脱臭装置。
(3)散水機構によって、散水する水の供給元となる貯水槽の水が、前記貯水槽と連結している充填層及び該充填層よりも上流の充填層の少なくとも1つに散水されることを特徴とする上記(2)の脱臭装置。
(4)散水機構によって、貯水槽の水が、さらに前記貯水槽と連結している充填層よりも下流の充填層に散水されることを特徴とする上記(3)の脱臭装置。
(5)充填層と充填層の間及び/又は充填層と貯水槽の間に、緩衝室を設けることを特徴とする上記(1)~(4)のいずれかの脱臭装置。
(6)充填材がpH6.5~8.5の発泡ガラスである上記(1)~(5)のいずれかの脱臭装置。
(7)最上流の充填層に導入する臭気ガスの温度を45℃以下に冷却する冷却装置を備えることを特徴とする請求項1~6のいずれか記載の脱臭装置。
(8)少なくとも1つの充填層を内部に有する充填塔が横方向に複数配置され、前記充填塔それぞれの下方に貯水槽が配置され、散水機構により前記充填塔内に散水された水が散水された前記充填塔の下方の貯水槽に、前記充填塔内の前記充填層を通過して導入されるように、前記充填塔と前記貯水槽が配置された上記(1)~(7)のいずれかの脱臭装置。
かつ、
(9)pHが6.5~8.5である脱臭に用いるための微生物担持用発泡ガラス。
(10)臭気ガスの脱臭方法であって、
臭気ガスを通過させ脱臭するための微生物を担持した充填材が充填された複数の充填層、微生物を培養するための複数の貯水槽及び前記充填層に前記貯水槽の水を散水するための散水機構を用意し、
前記充填層を、前記臭気ガスが導入される最上流の充填層から前記臭気ガスが排出される最下流の充填層まで、前記臭気ガスが流れるように連結させ、
前記貯水槽を、前記水が供給される最上流の貯水槽から最下流の貯水槽まで、前記水が流れるように連結させ、
前記充填層に臭気ガスを導入し、前記貯水槽に水を供給して、
前記最上流の貯水槽より下流の少なくとも1つの貯水槽の水を前記充填層に散水し、
散水する水の供給元となる貯水槽より上流の貯水槽に、充填層を通過した散水された水を導入する脱臭方法。
(11)臭気ガスの温度を45℃以下に冷却した後、充填層に前記臭気ガスを導入することを特徴とする請求項10記載の脱臭方法。
(12)微生物資材を貯水槽に導入することを特徴とする上記(10)又は(11)の脱臭方法。
That is, the present invention is specified by the matters shown below.
(1) A deodorizing device comprising a plurality of filling layers for passing odorous gas and deodorizing, a plurality of water tanks for culturing microorganisms, and a water spraying mechanism for spraying water in the water tanks on the filling layers. There is
The filling layer is filled with a filling material carrying microorganisms,
The packed bed is connected so that the malodorous gas flows from the most upstream packed bed into which the odorous gas is introduced to the most downstream packed bed from which the odorous gas is discharged,
The water tank is connected so that the water flows from the most upstream water tank to which the water is supplied from the outside of the deodorizing device to the most downstream water tank,
The water sprinkling mechanism is a mechanism for sprinkling water in at least one water tank downstream from the most upstream water tank to the filling layer,
A deodorizing device in which the filling layer and the water tank are connected so that the sprinkled water that has passed through the filling layer is introduced into the water tank upstream of the water tank serving as the supply source of the water to be sprinkled.
(2) The water tank serving as the supply source of water to be sprinkled and the water tank upstream from the water tank are arranged so that the water tank on the downstream side of the adjacent water tank is higher than the packed bed connected to the water tank on the upstream side. The deodorizing device according to (1) above, which is connected to a downstream packed bed.
(3) Water in a water storage tank, which is a supply source of water to be sprinkled, is sprinkled by a water sprinkling mechanism on at least one of a packed bed connected to the water tank and a packed bed upstream of the packed bed. The deodorizing device according to (2) above, characterized by:
(4) The deodorizing apparatus according to (3) above, wherein the water in the water tank is sprinkled by the water sprinkling mechanism onto a packed bed downstream of the packed bed connected to the water tank.
(5) The deodorizing device according to any one of (1) to (4) above, characterized in that a buffer chamber is provided between the packed bed and/or between the packed bed and the water tank.
(6) The deodorizing device according to any one of (1) to (5) above, wherein the filler is foamed glass having a pH of 6.5 to 8.5.
(7) The deodorizing apparatus according to any one of claims 1 to 6, further comprising a cooling device for cooling the temperature of the odorous gas introduced into the most upstream packed bed to 45°C or less.
(8) A plurality of packed towers having at least one packed bed inside are arranged in the horizontal direction, water tanks are arranged below each of the packed towers, and water sprinkled in the packed towers is sprinkled by a sprinkler mechanism. Any one of the above (1) to (7), wherein the packed tower and the water tank are arranged so that the water is introduced into the water tank below the packed tower through the packed bed in the packed tower. A deodorizing device.
And,
(9) Microorganism-carrying foam glass for use in deodorizing, having a pH of 6.5 to 8.5.
(10) A method for deodorizing odorous gas,
A plurality of packed beds filled with a filler supporting microorganisms for passing odorous gas and deodorizing, a plurality of water tanks for culturing the microorganisms, and water sprinkling for spraying the water of the water tanks on the packed beds. prepare the mechanism
connecting the packed bed so that the odorous gas flows from the most upstream packed bed into which the odorous gas is introduced to the most downstream packed bed from which the odorous gas is discharged;
connecting the water tanks so that the water flows from the most upstream water tank to which the water is supplied to the most downstream water tank;
introducing an odorous gas into the packed bed and supplying water to the water tank,
Sprinkling water in at least one water tank downstream from the most upstream water tank to the packed bed,
A deodorizing method of introducing sprinkled water that has passed through a filling layer into a water storage tank upstream of a water storage tank that supplies the water to be sprinkled.
(11) The deodorizing method according to claim 10, characterized in that after the temperature of the odorous gas is cooled to 45°C or less, the odorous gas is introduced into the packed bed.
(12) The deodorizing method according to (10) or (11) above, characterized in that the microbial material is introduced into a water tank.

本発明の脱臭装置及び脱臭方法は、優れた脱臭性能を有する。本発明の脱臭装置及び脱臭方法は、コンパクトな脱臭装置を提供できる。また、本発明の脱臭装置及び脱臭方法は、脱臭に要する費用を低減できる。 The deodorizing device and deodorizing method of the present invention have excellent deodorizing performance. The deodorizing device and deodorizing method of the present invention can provide a compact deodorizing device. Moreover, the deodorizing apparatus and deodorizing method of the present invention can reduce the cost required for deodorizing.

図1は、本発明の脱臭装置の一実施形態を示す図である。FIG. 1 is a diagram showing one embodiment of the deodorizing device of the present invention. 図2は、本発明の脱臭装置の他の一実施形態を示す図である。FIG. 2 is a diagram showing another embodiment of the deodorizing device of the present invention.

本発明の脱臭装置は、臭気ガスを通過させ脱臭するための複数の充填層、微生物を培養するための複数の貯水槽及び前記充填層に前記貯水槽の水を散水するための散水機構を備えた脱臭装置であって、前記充填層には、微生物を担持した充填材が充填され、前記充填層は、前記臭気ガスが導入される最上流の充填層から前記臭気ガスが排出される最下流の充填層まで、前記臭気ガスが流れるように連結され、前記貯水槽は、前記脱臭装置の外部より前記水が供給される最上流の貯水槽から最下流の貯水槽まで、前記水が流れるように連結され、前記散水機構は、前記最上流の貯水槽より下流の少なくとも1つの貯水槽の水を前記充填層に散水する機構であり、散水する水の供給元となる貯水槽より上流の貯水槽に、充填層を通過した散水された水が導入されるように、前記充填層と前記貯水槽が連結されている脱臭装置である。本発明の脱臭装置は、複数の充填層、すなわち2つ又は3つ以上の充填層を備え、本発明の脱臭装置に導入された臭気ガスは、複数の充填層を順次通過して排出される。臭気ガスが最初に通過する充填層を最上流の充填層といい、臭気ガスが最後に通過する充填層を最下流の充填層という。例えば、コンポストからの排気(臭気ガス)は、温度が80℃以上になることがあり、微生物が死滅するおそれがあるため、必要に応じて充填層に導入する臭気ガスを冷却してもよく、本発明の脱臭装置に臭気ガスの冷却装置を取り付けてもよい。冷却装置により、最上流の充填層に導入する臭気ガスの温度を45℃以下に冷却するのが好ましく、40℃以下に冷却するのがより好ましい。導入する臭気ガスの温度は15~45℃に調整することが好ましく、30~40℃に調整することがより好ましい。本発明の脱臭装置は、複数の貯水槽、すなわち2つ又は3つ以上の貯水槽を備え、本発明の脱臭装置に供給された水は、複数の貯水槽を順次通過する。水が最初に通過する貯水槽を最上流の貯水槽といい、水が最後に通過する貯水槽を最下流の貯水槽という。水が余分となった場合は、最下流の貯水槽から排出されてもよい。本発明の脱臭装置は、散水機構を備える。本発明における散水機構は、貯水槽の水を充填層に散水できれば、その構造等特に制限されるものではないが、例えば、貯水槽の水を汲み上げて充填層の上方まで送るポンプ、貯水槽から充填層の上方まで水を移送する配管、水を充填層に散水するノズル等で構成される。 The deodorizing apparatus of the present invention comprises a plurality of filling layers for passing odorous gases to deodorize, a plurality of water tanks for culturing microorganisms, and a water sprinkling mechanism for spraying water from the water tanks onto the filling layers. In the deodorizing apparatus, the packed bed is filled with a packing material supporting microorganisms, and the packed bed is arranged from the most upstream packed bed into which the malodorous gas is introduced to the most downstream packed bed where the malodorous gas is discharged. and the water tanks are arranged so that the water flows from the most upstream water tank to which the water is supplied from the outside of the deodorizing apparatus to the most downstream water tank. , and the water sprinkling mechanism is a mechanism for sprinkling water in at least one water tank downstream from the most upstream water tank to the filling layer, and water storage upstream from the water tank serving as a supply source of the water to be sprinkled. In the deodorizing apparatus, the packed bed and the water tank are connected so that sprinkled water that has passed through the packed bed is introduced into the tank. The deodorizing device of the present invention comprises a plurality of packed beds, i.e., two or more packed beds, and the odorous gas introduced into the deodorizing device of the present invention sequentially passes through the plurality of packed beds and is discharged. . The packed bed through which the odorous gas first passes is called the most upstream packed bed, and the packed bed through which the odorous gas passes last is called the most downstream packed bed. For example, the exhaust gas (odorous gas) from the compost may have a temperature of 80° C. or higher, which may kill the microorganisms. An odor gas cooling device may be attached to the deodorizing device of the present invention. The temperature of the odorous gas introduced into the most upstream packed bed is preferably cooled to 45°C or lower, more preferably 40°C or lower, by a cooling device. The temperature of the odorous gas to be introduced is preferably adjusted to 15 to 45°C, more preferably 30 to 40°C. The deodorizing apparatus of the present invention has a plurality of water tanks, that is, two or more water tanks, and the water supplied to the deodorizing apparatus of the present invention sequentially passes through the plurality of water tanks. The first water tank is called the uppermost water tank, and the last water tank is called the most downstream water tank. Any excess water may be drained from the most downstream reservoir. The deodorizing device of the present invention has a sprinkler mechanism. The structure of the water sprinkling mechanism in the present invention is not particularly limited as long as it can sprinkle the water in the water tank onto the packed bed. It consists of a pipe for transferring water to the upper part of the packed bed, a nozzle for spraying water on the packed bed, and so on.

本発明における充填層は、最上流の充填層から最下流の充填層まで、臭気ガスが流れるように連結されている。ここで連結とは、1つの充填層を通過した臭気ガスが、次の充填層に流れるように充填層と充填層がつながっていることを意味する。その構造は特に制限されず、例えば、臭気ガスを流すための配管で充填層と充填層との間をつなぐ、空間を介して充填層と充填層とを並べ、その空間を通じて臭気ガスを流す等の構造を挙げることができる。本発明における貯水槽は、最上流の貯水槽から最下流の貯水槽まで、水が流れるように連結されている。ここで連結とは、1つの貯水槽に貯留された水が、次の貯水槽に流れるように貯水槽と貯水槽がつながっていることを意味する。その構造は特に制限されず、例えば、水を流すための配管で貯水槽と貯水槽との間をつなぐ、壁を介して貯水槽と貯水槽とを並べ壁に穴をあけて水の通路とする、壁を介して貯水槽と貯水槽とを並べて貯水槽と壁の上方に空間を設け、空間を通じて壁の上部からオーバーフローした水を隣の貯水槽に流す構造等を挙げることができる。本発明においては、最上流の貯水槽より下流の少なくとも1つの貯水槽の水が、散水機構によって充填層に散水される。散水する水を供給する貯水槽は、1つでもよく2つ以上でもよい。散水される充填層は、1つでもよく2つ以上でもよく全ての充填層でもよい。また、最上流の貯水槽より下流の貯水槽の水が散水されれば、それに加えて最上流の貯水槽の水が散水されてもよい。本発明における充填層と貯水槽は、少なくとも散水する水の供給元となる貯水槽より上流の貯水槽に、充填層を通過した散水された水(以下、「処理水」ともいう。)が導入されるように連結されている。ここで連結とは、充填層を通過した水が貯水槽に導入されるように充填層と貯水槽がつながっていることを意味する。その構造は特に制限されず、例えば、水を流すための配管で充填層と貯水槽との間をつなぐ、充填層の下方に空間を介して貯水槽を設け、空間を通じて充填層を通過した水を貯水槽に落下させる等の構造を挙げることができる。本発明における充填層と貯水槽は、充填層に散水する水の供給元となる貯水槽より上流の貯水槽の少なくとも1つに、少なくとも1つの充填層を通過した処理水が導入されるように連結されていれば、各充填層を通過した処理水がどの貯水槽に導入されるかは、特に制限されるものではなく、貯水槽と連結されない充填層があってもよく、水の供給元となる貯水槽に処理水が導入されてもよく、水の供給元となる貯水槽より下流の貯水槽に処理水が導入されてもよい。 The packed bed in the present invention is connected so that odorous gas flows from the most upstream packed bed to the most downstream packed bed. Here, the connection means that the packed layers are connected so that the odorous gas that has passed through one packed layer flows to the next packed layer. The structure is not particularly limited. For example, a pipe for flowing odorous gas connects between the packed layers, the packed layers are arranged with a space therebetween, and the odorous gas is passed through the space. structure can be mentioned. The water tanks in the present invention are connected so that water flows from the most upstream water tank to the most downstream water tank. Here, the connection means that the water tanks are connected so that the water stored in one water tank flows into the next water tank. The structure is not particularly limited. Alternatively, a structure may be mentioned in which water tanks are arranged side by side with a wall interposed therebetween, a space is provided above the water tank and the wall, and water overflowing from the upper part of the wall flows through the space to the adjacent water tank. In the present invention, the water in at least one water tank downstream of the most upstream water tank is sprinkled onto the packed bed by the sprinkler mechanism. One or two or more water tanks for supplying water for sprinkling may be used. The number of packed beds to be watered may be one, two or more, or all packed beds. In addition, if the water in the water tank downstream of the most upstream water tank is sprinkled, the water in the most upstream water tank may be sprinkled. The packed bed and the water tank in the present invention are such that the sprinkled water that has passed through the packed bed (hereinafter also referred to as "treated water") is introduced into the water tank upstream of at least the water tank that supplies the water to be sprinkled. are connected so that Here, the connection means that the packed bed and the water tank are connected so that the water that has passed through the packed bed is introduced into the water tank. The structure is not particularly limited. can be dropped into a water tank. The packed bed and the water tank in the present invention are such that the treated water that has passed through at least one packed bed is introduced into at least one of the water tanks upstream of the water tank serving as the water supply source for watering the packed bed. As long as they are connected, there is no particular restriction as to which water tank the treated water that has passed through each packed bed is introduced into. The treated water may be introduced into the water tank that serves as the water supply source, or the treated water may be introduced into the water tank downstream of the water tank that serves as the water supply source.

本発明の脱臭装置は、少なくとも1つの充填層を内部に有する充填塔が横方向に複数配置され、前記充填塔それぞれの下方に貯水槽が配置され、散水機構により前記充填塔内に散水された水が散水された前記充填塔の下方の貯水槽に、前記充填塔内の前記充填層を通過して導入されるように、前記充填塔と前記貯水槽が、配置されてもよい。本発明における充填塔は、1つ又は2つ以上の充填層を内部に有し、前記充填層を臭気ガスが通過できる構造であれば、その構造、形状等は特に制限されず、例えば、円筒状、角筒状等の形状を挙げることができ、これら筒形状物内に充填層を設けた構造等を挙げることができる。また、例えば、充填層が1つの場合は1つの充填層を臭気ガスが通過でき、充填層が2つ以上の場合は順次各充填層を臭気ガスが通過できる構造を挙げることができる。例えば、複数の充填層を、充填層と充填層の間に、臭気ガスが通過できる空間を設けて充填塔内に配置してもよい。本実施形態においては、2つ以上の充填塔が横方向に並んで配置され、充填塔間を臭気ガスが流れるように連結し、最上流の充填層を有する充填塔への臭気ガス導入部を設け、最下流の充填層を有する充填塔からの臭気ガス排出部を設けることにより、各充填層が、臭気ガスが導入される最上流の充填層から前記臭気ガスが排出される最下流の充填層まで、臭気ガスが流れるように連結される。本実施形態においては、貯水槽が、それぞれの充填塔の下方に配置される。貯水槽は、1つの充填塔に対して1つ配置して、1つの充填塔を通過した散水が1つの貯水槽に導入されるようにしてもよく、複数の充填塔に対して1つ配置して、複数の充填塔を通過した散水が1つの貯水槽に導入されるようにしてもよい。貯水槽間を水が流れるように連結し、最上流の貯水槽への水供給部を設けることにより、各貯水槽が、水が供給される最上流の貯水槽から最下流の貯水槽まで、水が流れるように連結される。最下流の貯水槽には、必要に応じて水の排出部を設けてもよい。本態様の脱臭装置は、充填塔内に設けられた充填層が縦方向に並ぶように各充填塔が縦に設置され、縦に設置された充填塔が複数横方向に並べられている。そのため、充填塔に散水された水は、臭気ガスと同じ経路を通って下方に落下して、充填塔の下方に配置された貯水槽に導入される。 In the deodorizing apparatus of the present invention, a plurality of packed towers having at least one packed bed inside are arranged in the horizontal direction, water tanks are arranged below each of the packed towers, and water is sprinkled into the packed towers by a water spraying mechanism. The packed tower and the water tank may be arranged such that water is introduced into the sprinkled water tank below the packed tower through the packed bed in the packed tower. The packed tower in the present invention is not particularly limited in its structure, shape, etc., as long as it has one or two or more packed layers inside and the odorous gas can pass through the packed layers. Shapes such as a shape and a rectangular tube shape can be mentioned, and a structure in which a filling layer is provided in the cylindrical shape can be mentioned. Further, for example, when there is one packed layer, the odorous gas can pass through one packed layer, and when there are two or more packed layers, the odorous gas can pass through each packed layer sequentially. For example, a plurality of packed beds may be arranged in a packed tower with spaces between the packed beds through which the odorous gas can pass. In this embodiment, two or more packed towers are arranged side by side in the horizontal direction, the packed towers are connected so that odorous gas flows, and the odorous gas introduction part to the packed tower having the most upstream packed bed is provided. By providing an odorous gas discharge part from the packed tower having the most downstream packed bed, each packed bed is connected to the most downstream packed bed to which the odorous gas is discharged from the most upstream packed bed to which the malodorous gas is introduced. The layers are fluidly connected to the odor gas. In this embodiment, a water tank is arranged below each packed tower. One water tank may be arranged for one packed tower so that sprinkled water passing through one packed tower is introduced into one water tank, or one water tank may be arranged for a plurality of packed towers. Then, sprinkled water that has passed through a plurality of packed towers may be introduced into one water tank. By connecting the water tanks so that water flows and providing a water supply part to the most upstream water tank, each water tank can be supplied with water from the most upstream water tank to the most downstream water tank, connected for water flow. The most downstream water tank may be provided with a water discharge section as required. In the deodorizing apparatus of this embodiment, each packed tower is installed vertically so that the packed beds provided in the packed tower are arranged in the vertical direction, and a plurality of vertically installed packed towers are arranged in the horizontal direction. Therefore, the water sprinkled on the packed tower falls through the same path as the odorous gas and is introduced into the water tank arranged below the packed tower.

本発明における貯水槽には、充填層に散水され充填層を通過した水である処理水が導入される。この処理水は、充填層を通過する間に充填層中の微生物の一部を含むようになるため、貯水槽の水に微生物が導入される。また処理水は、充填層を通過する間にアンモニア等の微生物にとって栄養分となる臭気ガス中の成分を含むようになるため、微生物にとっての栄養分も貯水槽の水に導入される。このため、貯水槽で微生物を培養することが可能となるが、1つの貯水槽のみを設けた場合、微生物が十分培養され増殖しないうちに貯水槽の水が再び充填層に散水されるので、微生物の培養効果を発揮することはできない。本発明では、複数の貯水槽を設け、水が貯水槽間を上流から下流に流れるようにするため、微生物を含んだ水は、各貯水槽で貯留され次の貯水槽へと流れていく。そのため、下流の貯水槽に貯留されるまでの間に微生物の培養、増殖に必要な時間を確保することができる。そして本発明では、最上流ではなく下流の貯水槽まで流れてきた水を再び充填層に散水し、かつ散水する水の供給元となる貯水槽より上流の貯水槽に処理水が導入されるため、上流の貯水槽に導入された処理水中の微生物は、散水する水の供給元となる貯水槽に流れてくるまでの間に、十分培養され増殖する。そのため本発明では、微生物を多く含んだ水を充填層に散水することができ、充填層での臭気成分の分解を促進することができる。一般に、微生物は環境が整うと倍数でなく乗数で増えると言われており、有機分解(脱臭)能力は微生物の数に比例するので、本発明において微生物を含んだ水を各貯水槽間を移動させながら微生物を培養し増殖させることによる効果は極めて大きくなる。貯水槽で培養される微生物は、処理水に含まれる微生物のみでなく、予め貯水槽の水中に微生物を添加してもよく、脱臭装置の運転途中で貯水槽の水中に微生物を添加して補充してもよい。また、本発明においては、最上流の充填層に臭気ガスを導入する前に、処理水を臭気ガスに散水してもよい。散水された後の処理水は、微生物の栄養分と共に溶存酸素を多く含むので、微生物の培養により好適となる。 Treated water, which is water sprinkled on the packed bed and passed through the packed bed, is introduced into the water tank in the present invention. Since this treated water contains some of the microorganisms in the packed bed while passing through the packed bed, the microorganisms are introduced into the water in the water tank. In addition, since the treated water contains odorous gas components such as ammonia that are nutrients for microorganisms while passing through the packed bed, nutrients for microorganisms are also introduced into the water in the water tank. Therefore, it is possible to culture microorganisms in the water tank, but if only one water tank is provided, the water in the water tank will be sprayed again on the filling layer before the microorganisms are sufficiently cultured and propagated. The effect of culturing microorganisms cannot be exhibited. In the present invention, since a plurality of water tanks are provided and water flows between the water tanks from upstream to downstream, water containing microorganisms is stored in each water tank and flows to the next water tank. Therefore, it is possible to secure the time necessary for culturing and growing the microorganisms until they are stored in the downstream water tank. And in the present invention, the water that has flowed to the downstream water tank instead of the most upstream water tank is sprinkled again on the packed bed, and the treated water is introduced into the water tank upstream of the water tank that supplies the water to be sprinkled. , the microorganisms in the treated water introduced into the upstream water tank are sufficiently cultured and proliferate until they flow into the water tank serving as the supply source of water to be sprinkled. Therefore, in the present invention, water containing a large amount of microorganisms can be sprinkled on the packed bed, and the decomposition of odorous components in the packed bed can be promoted. In general, it is said that microorganisms increase not by multiples but by multipliers when the environment is improved, and the organic decomposition (deodorization) ability is proportional to the number of microorganisms. The effect of culturing and growing microorganisms while allowing them to grow is extremely large. The microorganisms cultured in the water tank are not limited to the microorganisms contained in the treated water, but may be added in advance to the water in the water tank. You may Further, in the present invention, treated water may be sprinkled onto the odorous gas before introducing the odorous gas into the most upstream packed bed. The treated water after watering contains nutrients for microorganisms and a large amount of dissolved oxygen, so it is more suitable for culturing microorganisms.

本発明における充填層は、微生物を担持した充填材が充填された充填層である。臭気ガスは、充填層を通過する際、臭気成分が充填材に担持された微生物により分解されて脱臭される。微生物としては、アンモニア等の臭気成分を分解する微生物であれば特に制限されず、例えば、アンモニア硝化菌等を挙げることができる。充填材としては、微生物を担持できるものであれば特に制限されず、例えば、ロックウール、発泡ガラス、その他の多孔質材等を挙げることができる。従来、発泡ガラスは脱臭のための微生物の担体としては多くは使用されてこなかった。これは、発泡ガラスのpHは10~11程度のアルカリ性であるのに対し、脱臭に使用される微生物はpHが中性の環境でないと、効率的な活動を行わないため、膨大な量のガラス発泡材を使用するか、またはたとえば一定期間散水を行いpHを下げて使用する必要があったからである。発泡ガラスを脱臭のための微生物の担体として使用しようという発想はあったがこのような問題が普及の障害になっていた。しかし、発泡ガラスであってもpHを6.5~8.5程度にすれば、脱臭のための微生物の担体として従来の担体よりもはるかに優れることを見いだした。このpHが6.5~8.5である脱臭に用いるための微生物担持用発泡ガラスは、従来はなかったものである。発泡ガラスのpHは、発泡ガラスの比重から割り出した1Lの体積分の重量の発泡ガラスを、2Lのビーカーに入れ、1Lの中性(pH7±0.1)の水を加えて10分攪拌し、その後静置して24時間経過後、水のpHをpH測定器で測定することにより測定でき、本発明における発泡ガラスのpHとは、前記方法で測定したpHをいう。発泡ガラスは、ガラスや添加物などの原材料を700~1000℃で焼成し、焼成物を粉砕して得られる多孔材料であるため、発泡ガラス表面には粉砕の際に生じる微細な粉状成分が付着している。発泡ガラスのpHは、発泡ガラスから溶出する成分と、発泡ガラス表面に付着した前記微細な粉状成分に影響される。発泡ガラスのpHを6.5~8.5にすることにより、溶出成分や付着成分の影響により脱臭に使用される微生物の活動が低下することを防ぐことができる。より微生物の活動低下を防ぎ、微生物の活動をより向上させる観点から、発泡ガラスのpHは、6.5~8.0がより好ましく、6.5~7.5が更に好ましい。また、pHが6.5~8.5である発泡ガラスは、発泡ガラスを無機酸等の酸で洗浄することにより得ることができる。本発明の微生物担持用発泡ガラスは、脱臭という用途を見いだした用途発明である。特に、糞尿のコンポスト等の畜産施設からの臭気ガスの脱臭用途を見いだしたものである。本発明における充填材は、pHが6.5~8.5である発泡ガラスが好ましい。また、貯水槽の中に、微生物の培養を助けるためにpHが6.5~8.5の発泡ガラスを入れてもよい。充填材としてロックウールを使用した場合、ロックウールが散水により水分を含むとひしゃげてしまい、空気が通りにくくなる。通常、3ケ月程度でこのような状況が発生するため、性能維持のために半年~1年程度で交換が必要になる。一方、発泡ガラスは形状の変化や劣化がおきにくいので、脱臭のための微生物の担体(充填材)として発泡ガラスを使用できると、充填材交換のためのランニングコストを低減できる。 The packed bed in the present invention is a packed bed filled with a filler carrying microorganisms. When the odorous gas passes through the filling layer, the odorous components are decomposed by the microorganisms supported on the filling material and deodorized. Microorganisms are not particularly limited as long as they decompose odorous components such as ammonia, and examples thereof include ammonia nitrifying bacteria. The filler is not particularly limited as long as it can support microorganisms, and examples thereof include rock wool, foam glass, and other porous materials. Conventionally, foam glass has not been widely used as a carrier for microorganisms for deodorization. This is because the pH of foamed glass is about 10 to 11, which is alkaline, and the microorganisms used for deodorization do not work efficiently unless the pH is in a neutral environment. This is because it has been necessary to use a foamed material or, for example, to lower the pH by sprinkling water for a certain period of time. There was an idea to use foam glass as a carrier for microorganisms for deodorization, but such a problem hindered its popularization. However, it has been found that even foam glass is far superior to conventional carriers as a carrier for microorganisms for deodorization if the pH is adjusted to about 6.5 to 8.5. Microorganism-carrying foam glass for use in deodorization with a pH of 6.5 to 8.5 has never existed before. The pH of the foam glass was measured by putting 1 L volume of foam glass calculated from the specific gravity of the foam glass into a 2 L beaker, adding 1 L of neutral (pH 7±0.1) water, and stirring for 10 minutes. After 24 hours of standing, the pH of the water can be measured with a pH meter. The pH of the foamed glass in the present invention refers to the pH measured by the above method. Foam glass is a porous material obtained by firing raw materials such as glass and additives at 700 to 1000°C and pulverizing the fired product. Adhering. The pH of foam glass is influenced by components eluted from the foam glass and the fine powdery components adhering to the surface of the foam glass. By adjusting the pH of the foamed glass to 6.5 to 8.5, it is possible to prevent the activity of microorganisms used for deodorizing from decreasing due to the influence of eluted components and adhered components. The pH of the foam glass is more preferably 6.5 to 8.0, and even more preferably 6.5 to 7.5, from the viewpoint of preventing a decrease in microbial activity and further improving microbial activity. A foam glass having a pH of 6.5 to 8.5 can be obtained by washing the foam glass with an acid such as an inorganic acid. The foamed glass for supporting microorganisms of the present invention is a use invention that finds a use for deodorizing. In particular, it has been found to be used for deodorizing odorous gases from animal husbandry facilities such as manure compost. The filler in the present invention is preferably foamed glass having a pH of 6.5 to 8.5. Foam glass with a pH of 6.5-8.5 may also be placed in the reservoir to aid in culturing the microorganisms. When rock wool is used as a filler, it is crushed when water is sprinkled on the rock wool, making it difficult for air to pass through. Normally, such a situation occurs in about three months, so replacement is required in about six months to one year to maintain performance. On the other hand, since foam glass is less likely to change shape or deteriorate, if foam glass can be used as a carrier (filler) for microorganisms for deodorizing, the running cost for replacing the filler can be reduced.

本発明では、散水する水の供給元となる貯水槽及び前記貯水槽より上流の貯水槽は、隣り合う貯水槽の下流側の貯水槽が、上流側の貯水槽に連結されている充填層よりも下流の充填層に連結されていることが好ましい。充填層を通過する臭気ガス中の臭気成分の濃度は、上流が濃く下流にいくにしたがって薄くなっていく。したがって、処理水に含まれる微生物にとって栄養分となる成分の濃度も上流の充填層からの処理水では濃く、下流にいくにしたがって薄くなっていく。そのため、隣り合う貯水槽のうち下流側の貯水槽が連結される充填層が、上流側の貯水槽が連結される充填層よりも下流の充填層となるようにすることにより、下流の貯水槽には上流の貯水槽に比べて微生物にとっての栄養分の少ない処理水が導入され、反対に上流の貯水槽には栄養分の多い処理水が導入される。栄養分の多い上流の貯水槽で増殖した微生物は、下流の貯水槽に運ばれると、栄養分が少ないため飢餓状態になる。飢餓状態の微生物は栄養分を見つけると最も活発な分解活動を行うため、飢餓状態の微生物を含む水を充填層に散水すると、充填層において微生物が臭気成分の分解活動を活発に行うことにより脱臭効果を更に促進することができる。また、貯水槽に導入される処理水中の栄養分は、下流にいくにしたがい段階的に少なくなるため、栄養分が一気に減少することにより微生物が減少するのを防ぐことができる。散水する水の供給元となる貯水槽より下流での充填層と貯水槽との処理水の導入に関する対応関係は、特に制限されない。 In the present invention, the water tank serving as the supply source of the water to be sprinkled and the water tank upstream from the water tank are arranged such that the water tank on the downstream side of the adjacent water tank is connected to the water tank on the upstream side from the packed bed. is also preferably connected to the downstream packed bed. The concentration of odorous components in the odorous gas passing through the packed bed is high upstream and becomes thinner as it goes downstream. Therefore, the concentration of the components that serve as nutrients for the microorganisms contained in the treated water is also high in the treated water from the upstream packed bed, and becomes thinner as it goes downstream. Therefore, the filling layer to which the downstream water tank is connected among the adjacent water tanks is arranged to be a downstream filling layer from the filling layer to which the upstream water tank is connected. Treated water containing less nutrients for microorganisms than the upstream water tank is introduced into the water tank, and conversely, treated water containing more nutrients is introduced into the upstream water tank. Microorganisms that grow in nutrient-rich upstream reservoirs are starved when transported to downstream reservoirs, where nutrients are scarce. Since starved microorganisms are most active in decomposition when they find nutrients, when water containing starved microorganisms is sprinkled on the packed bed, the microorganisms in the packed bed actively decompose odorous components, resulting in a deodorizing effect. can be further promoted. In addition, since the nutrients in the treated water introduced into the water tank gradually decrease as it goes downstream, it is possible to prevent the microorganisms from decreasing due to the sudden decrease in nutrients. There is no particular restriction on the relationship regarding the introduction of treated water between the packed bed and the water tank downstream of the water tank serving as the supply source of water to be sprinkled.

本発明では、散水機構によって、散水する水の供給元となる貯水槽の水が、前記貯水槽と連結している充填層及び該充填層よりも上流の充填層の少なくとも1つに散水されることが好ましい。こうすることにより、臭気成分の分解効果の高い下流の貯水槽の水を、臭気成分を多く含む臭気ガスが通過する上流の充填層に散水することができ、臭気成分の分解効率を高めることができる。さらに、本発明では、上記に加えて、散水する水の供給元となる他の貯水槽の水が、前記貯水槽と連結している充填層よりも下流の充填層の少なくとも1つに散水されてもよい。こうすることにより、臭気成分の分解効果の高い下流の貯水槽の水を、臭気成分を多く含む臭気ガスが通過する上流の充填層に散水し、臭気成分の分解効果の低い上流の貯水槽の水を、臭気成分の量が少ない臭気ガスが通過する下流の充填層に散水して、負荷を均一化して分解処理の効率化を図ることができる。本発明における散水量は特に制限されるものではないが、例えば、充填層の体積1mあたりの散水量が0.02~0.1m/分等を挙げることができる。 In the present invention, the water sprinkling mechanism sprinkles the water in the water tank, which is the source of the water to be sprinkled, onto at least one of the packed bed connected to the water tank and the packed bed upstream of the packed bed. is preferred. By doing so, the water in the downstream storage tank, which is highly effective in decomposing malodorous components, can be sprinkled onto the upstream packed bed through which the odorous gas containing a large amount of malodorous components passes, thereby increasing the efficiency of decomposing malodorous components. can. Furthermore, in the present invention, in addition to the above, water in another water tank serving as a supply source of water to be sprinkled is sprinkled on at least one of the packed beds downstream of the packed bed connected to the water tank. may By doing so, the water in the downstream water storage tank, which is highly effective in decomposing odorous components, is sprinkled onto the upstream filled layer through which the odorous gas containing many odorous components passes, and the water in the upstream water storage tank, which is less effective in decomposing odorous components, is sprayed. Water can be sprayed on the downstream packed bed through which the odorous gas having a small amount of odorous components passes to equalize the load and improve the efficiency of the decomposition treatment. Although the amount of water sprayed in the present invention is not particularly limited, for example, the amount of water sprayed per 1 m 3 of packed bed volume can be 0.02 to 0.1 m 3 /min.

本発明では、充填層と充填層の間及び/又は充填層と貯水槽の間に、緩衝室を設けることが好ましい。本発明では、臭気ガスを複数の充填層を通過させて流すために、相当の圧力をかけて臭気ガスを脱臭装置に導入する必要があり、充填層に圧力が偏ってかかるおそれがある。そのため、充填層にかかる圧力を均一化することが好ましい。充填層と充填層の間に気流圧力のバッファとなる緩衝室を設けることにより、充填層に入る臭気ガス気流の圧力を均一化することができる。また、充填層を通過した処理水は貯水槽に導入されるが、充填層を通過した臭気ガスも貯水槽の水面に当たる構造の場合、気流の圧力が均一でないと水面の特定個所に集中して気流が当たることにより、水が飛ばされたり、貯水槽から貯水槽への水の流れが乱されたりするおそれがある。そのため、貯水槽の水面に均一に気流が当たるようにすることが好ましい。充填層と貯水槽の間に気流圧力のバッファとなる緩衝室を設けることにより、貯水槽の水面に当たる臭気ガス気流の圧力を均一化することができる。緩衝室は、臭気ガス気流の圧力を均一化するための空間であり、臭気ガス気流が当たる充填層表面の面積や貯水槽水面の面積、及び導入する臭気ガスの流量や圧力に応じて、その容積を適宜選択できるが、臭気ガス気流が当たる充填層表面や貯水槽水面においては、これら表面積や水面の面積と同じ面積を有することが好ましい。また、臭気ガス気流の圧力を均一化するために、充填層と緩衝室との間、又は緩衝室の中に気流を均一化するための部材を置くことができる。前記部材としては、例えば、穴又はスリットのあいた板、メッシュ状の板等を挙げることができる。この緩衝室を処理水が通過する通路として使用すると、処理水中に溶存酸素を多く含ませることができ、微生物の培養のために、より効果的になる。養豚場等のコンポストの場合は、一般にヒーターが内蔵され、豚糞を強制的に発酵(堆肥化)する仕組みになっており、最も強烈な悪臭が発生するのは、発酵するまでの発酵過程であるコンポスト運転時である。発酵してしまうと、悪臭であることに変わりはないものの臭気は低減するが、一般のコンポストは、十分な発酵ができていない場合が少なくはなく、これも悪臭の原因になっている。本発明の脱臭装置は、臭気濃度に応じて(栄養源の増減に応じて)装置内の微生物が増減する構造になっているため、発酵過程の時間帯や発酵程度によって異なる悪臭の度合いに対して、広く対応できる。また、養豚等のコンポストに限らず有機物による悪臭であれば、どのようなものでも対応可能である。 In the present invention, it is preferred to provide a buffer chamber between the packed bed and/or between the packed bed and the reservoir. In the present invention, in order to flow the odorous gas through the plurality of packed beds, it is necessary to apply a considerable pressure to introduce the odorous gas into the deodorizing device, and there is a risk that the pressure will be unevenly applied to the packed beds. Therefore, it is preferable to equalize the pressure applied to the filling layer. By providing a buffer chamber that buffers the airflow pressure between the packed layers, the pressure of the odor gas stream entering the packed layers can be made uniform. In addition, the treated water that has passed through the packed bed is introduced into the water tank, but in the case of a structure in which the odorous gas that has passed through the packed bed hits the water surface of the water tank, if the pressure of the airflow is not uniform, it will concentrate at a specific point on the water surface. The airflow may blow the water or disturb the flow of water from one reservoir to another. Therefore, it is preferable that the water surface of the water tank is evenly exposed to the air current. By providing a buffer chamber between the filling layer and the water tank to buffer the airflow pressure, the pressure of the odor gas stream hitting the water surface of the water tank can be made uniform. The buffer chamber is a space for equalizing the pressure of the odorous gas stream. Although the volume can be appropriately selected, it is preferable that the surface of the packed bed and the water surface of the water tank, which are hit by the odorous gas stream, have the same surface area and the area of the water surface. Also, in order to equalize the pressure of the odorous gas stream, a member for equalizing the airflow can be placed between the packed bed and the buffer chamber or within the buffer chamber. Examples of the member include a plate with holes or slits, a mesh plate, and the like. When this buffer chamber is used as a passage through which the treated water passes, the treated water can contain a large amount of dissolved oxygen, which is more effective for culturing microorganisms. In the case of composting at pig farms, etc., a heater is generally built in, and the mechanism is such that the pig manure is forcibly fermented (composted). This is during a certain composting operation. If compost is fermented, the odor is still bad, but the odor is reduced. The deodorizing device of the present invention has a structure in which the number of microorganisms in the device increases or decreases according to the odor concentration (according to the increase or decrease of the nutrient source). can be widely used. In addition, not only compost from pig farming but also any odor caused by organic matter can be treated.

本発明における貯水槽には、微生物の栄養剤、pH調整剤等を加えてもよく、微生物を加えてもよい。栄養剤を加えることや、pHを微生物の培養に適したpHに調整することにより微生物の培養をより促進することができる。また、貯水槽に微生物を添加することにより、死滅や脱臭装置外への流出等により減少した微生物を補充し、貯水槽における又は充填層内における微生物の量を一定にすることができる。また、自然界では有機物には微量であってもそこに分解菌が存在し、又はそこに分解菌が飛来する。本発明の脱臭装置は、そのような微生物を増殖し活性化できるため、充填層や貯水槽に微生物を添加しなくても、そのような地場菌のみでも悪臭成分を分解することが可能な場合がある。貯水槽に間欠曝気等の曝気により酸素を供給して、微生物の培養を促進してもよい。本発明における貯水槽には、pH、EC(電気伝導率)、水温等の計測器、ヒーター、冷却器等の水温調整器などを設置して常時管理し、貯水槽の環境を微生物が増殖活性化するのに適した環境にすることが好ましい。ECを測定することにより貯水槽の汚濁の程度を測定できる。微生物は45℃を上回る高温では死滅するおそれがあり、15℃を下回る低温で働きが鈍化するので、貯水槽の水や臭気ガスの温度は、15~45℃が好ましく、15~40℃がより好ましく、30℃±3℃を更に好ましい温度として挙げることができる。また、本発明の脱臭装置では、臭気濃度、貯水槽の水量、風量、装置内の臭気ガス温度等の装置内温度、微生物の残量などを測定する測定器を設置してもよい。例えば、脱臭装置の排気管に風量計を設置することにより、脱臭装置の目詰まりを検知することができる。これらの測定値を管理し各条件を調製することにより、効率よく脱臭を行うことができると共に、トラブルの発生を未然に回避したり、発生したトラブルを速やかに解決したりすることができる。インターネット回線等を通じてこれらの測定値を管理すると、現地ユーザーと保守メンテナンス業者等との間でリアルタイムで情報を共有することができ、迅速な対応が可能となる。また、離れたところにある脱臭装置を一括して管理することができる。本発明の脱臭装置及び脱臭方法においては、微生物資材を貯水槽に導入してもよい。本発明における微生物資材とは、微生物の培養の促進、微生物からの酵素排出の促進を行う成分であり、例えば、フルボ酸、フミン酸等を挙げることができる。 Nutrients for microorganisms, pH adjusters and the like may be added to the water tank in the present invention, and microorganisms may be added. Cultivation of microorganisms can be further promoted by adding nutrients or adjusting the pH to a pH suitable for culturing microorganisms. In addition, by adding microorganisms to the water tank, it is possible to replenish the microorganisms that have decreased due to death or outflow to the outside of the deodorizing apparatus, and to keep the amount of microorganisms in the water tank or in the packed bed constant. Moreover, in the natural world, degrading bacteria exist in organic matter even if the amount is very small, or degrading bacteria fly there. Since the deodorizing device of the present invention can proliferate and activate such microorganisms, it is possible to decompose malodorous components only with such local bacteria without adding microorganisms to the filling bed or water tank. There is Cultivation of microorganisms may be promoted by supplying oxygen to the water tank by aeration such as intermittent aeration. In the water tank in the present invention, measuring instruments such as pH, EC (electrical conductivity), water temperature, etc., water temperature regulators such as heaters and coolers are installed and constantly managed, and the environment of the water tank is maintained so that microorganisms can proliferate. It is preferable to create an environment suitable for By measuring the EC, the degree of contamination of the water tank can be determined. Microorganisms may die at high temperatures above 45°C, and their activity slows down at low temperatures below 15°C. Preferably, 30°C ± 3°C can be mentioned as a more preferable temperature. In addition, the deodorizing apparatus of the present invention may be provided with a measuring instrument for measuring the concentration of odor, the amount of water in the water tank, the air flow, the internal temperature of the apparatus such as the temperature of the odorous gas in the apparatus, the remaining amount of microorganisms, and the like. For example, clogging of the deodorizing device can be detected by installing an air flow meter in the exhaust pipe of the deodorizing device. By managing these measured values and adjusting each condition, it is possible to efficiently deodorize, prevent the occurrence of troubles, and quickly solve the troubles that have occurred. If these measured values are managed through the Internet line, etc., information can be shared in real time between the local user and maintenance contractors, etc., and quick response becomes possible. In addition, it is possible to collectively manage deodorizing devices in remote locations. In the deodorizing device and deodorizing method of the present invention, the microbial material may be introduced into the water tank. The microbial material in the present invention is a component that promotes culturing of microorganisms and promotes enzyme excretion from microorganisms, and examples thereof include fulvic acid and humic acid.

本発明の一実施形態を、図1を用いて説明する。図1の脱臭装置では、充填層を縦に2つ並べ、その下方に貯水槽を設けたものを横に3列並べている。各充填層は最上流の充填層である第1充填層21から最下流の充填層である第6充填層42まで臭気ガスが流れるように、緩衝室で連結されている。また、各貯水槽は最上流の貯水槽である第1貯水槽101から最下流の貯水槽である第3貯水槽103まで水が流れるように、水通路で連結されている。また、第1充填層21に導入する前の臭気ガスに臭気ガス導入路11において処理水を散水している。図1の脱臭装置においては、臭気ガス導入路11における脱臭を第1脱臭、第1充填層21及び第2充填層22における脱臭を第2脱臭、第3充填層31及び第4充填層32における脱臭を第3脱臭、第5充填層41及び第6充填層42における脱臭を第4脱臭と呼んでいる。臭気ガスは、臭気ガス導入路11及び緩衝室S1aを通って第1充填層21に導入される。導入された臭気ガスは、第1充填層21を通過し、緩衝室S1bを通って、第2充填層22に導入され、第2充填層22を通過した臭気ガスは、緩衝室S1c及びS2cを通って、第3充填層31に導入され、第3充填層31を通過した臭気ガスは、緩衝室S2bを通って、第4充填層32に導入され、第4充填層32を通過した臭気ガスは、緩衝室S2a及びS3aを通って、第5充填層41に導入され、第5充填層41を通過した臭気ガスは、緩衝室S3bを通って、第6充填層42に導入され、第6充填層42を通過した臭気ガスは、緩衝室S3cを通って、臭気ガス排出路12から排出される。排出される脱臭されたガスの一部(例えば、20%程度)を臭気ガス導入路11に戻して、脱臭装置に導入される臭気ガスを薄め、処理する臭気ガス中の臭気成分の濃度を調整してもよい。また、処理する臭気ガスを冷却するために使用してもよい。 One embodiment of the present invention will be described with reference to FIG. In the deodorizing apparatus of FIG. 1, two packed beds are arranged vertically, and three rows of water tanks are arranged below them. Each packed layer is connected by a buffer chamber so that the odor gas flows from the first packed layer 21, which is the most upstream packed layer, to the sixth packed layer 42, which is the most downstream packed layer. Each water tank is connected by a water passage so that water flows from the first water tank 101, which is the most upstream water tank, to the third water tank 103, which is the most downstream water tank. In addition, treated water is sprinkled in the odor gas introduction passage 11 to the odor gas before it is introduced into the first filling layer 21 . In the deodorizing apparatus of FIG. 1, the deodorization in the odorous gas introduction path 11 is the first deodorization, the deodorization in the first filling layer 21 and the second filling layer 22 is the second deodorization, the third filling layer 31 and the fourth filling layer 32 are Deodorization is called third deodorization, and deodorization in the fifth and sixth filling layers 41 and 42 is called fourth deodorization. The odorous gas is introduced into the first filling layer 21 through the odorous gas introduction passage 11 and the buffer chamber S1a. The introduced odorous gas passes through the first filling layer 21, passes through the buffer chamber S1b, and is introduced into the second filling layer 22. After passing through the second filling layer 22, the odorous gas passes through the buffer chambers S1c and S2c. The odorous gas that has passed through the third packed layer 31 and passed through the third packed layer 31 is introduced into the fourth packed layer 32 through the buffer chamber S2b and passed through the fourth packed layer 32. is introduced into the fifth packing layer 41 through the buffer chambers S2a and S3a, and the odorous gas that has passed through the fifth packing layer 41 is introduced into the sixth packing layer 42 through the buffer chamber S3b, and is introduced into the sixth packing layer 42 through the buffer chamber S3b. The odorous gas that has passed through the filling layer 42 is discharged from the odorous gas discharge passage 12 through the buffer chamber S3c. A part (for example, about 20%) of the discharged deodorized gas is returned to the odor gas introduction path 11 to dilute the odor gas introduced into the deodorizing device and adjust the concentration of odor components in the odor gas to be treated. You may It may also be used to cool the odorous gas to be treated.

一方、水供給路13から第1貯水槽101に水が供給され、供給された水は水通路13-1を通って第2貯水槽102に流れ、第2貯水槽102の水は水通路13-2を通って第3貯水槽103に流れる。水通路13-1は、第1貯水槽101と第2貯水槽102との間の壁に水が通過できる穴をあけたものであり、水通路13-2は、第2貯水槽102、第3貯水槽103及びこれらの間の壁の上方の空間(緩衝室S2a及びS3aを兼ねている)において、第2貯水槽102の水を前記壁の上をオーバーフローさせて第3貯水槽103に流すものである。図1の脱臭装置では、水供給路13から適切な量の水を流し続けることにより、第1貯水槽101から第3貯水槽103への水の流れを作っている。また、余分な水は水排出路14から排出し、水が不足する場合は供給する水の量を増やすことにより水量の調整を行っている。 On the other hand, water is supplied from the water supply path 13 to the first water tank 101, the supplied water flows through the water passage 13-1 to the second water tank 102, and the water in the second water tank 102 flows into the water passage 13. -2 and flows into the third water tank 103 . The water passage 13-1 is formed by making a hole in the wall between the first water tank 101 and the second water tank 102 through which water can pass. 3. In the water tank 103 and the space above the wall between them (which also serves as buffer chambers S2a and S3a), the water in the second water tank 102 overflows the wall and flows to the third water tank 103. It is. In the deodorizing apparatus of FIG. 1 , water is made to flow from the first water tank 101 to the third water tank 103 by continuing to flow an appropriate amount of water from the water supply channel 13 . Moreover, excess water is discharged from the water discharge path 14, and when water is insufficient, the amount of water to be supplied is increased to adjust the amount of water.

第3貯水槽103の水は、散水用ポンプ71で汲み上げられ、散水路7を通って、散水ノズル72及び73から充填層に散水される。散水路7は途中で3つに分かれ、1つは第2充填層22、第3充填層31及び第6充填層42の上方に、1つは第1充填層21、第4充填層32及び第5充填層41の上方に、1つは臭気ガス導入路11の上方に通じている。図1の脱臭装置では、最下流の貯水槽である第3貯水槽103の水が、全ての充填層に散水されている。第2充填層22及び第1充填層21を通過した水は、緩衝室S1a(処理水通路を兼ねる)を通って下に落下することにより第1貯水槽101に導入される。同様に、第3充填層31及び第4充填層32を通過した水は、緩衝室S2a(処理水通路を兼ねる)を通って下に落下することにより第2貯水槽102に導入され、第6充填層42及び第5充填層41を通過した水は、緩衝室S3a(処理水通路を兼ねる)を通って下に落下することにより第3貯水槽103に導入される。図1の脱臭装置では、充填層を通過した水(処理水)が、散水する水の供給元となる第3貯水槽103より上流の貯水槽に導入されると共に、第3貯水槽103にも導入されている。また、第3貯水槽103並びにその上流の貯水槽101及び102では、隣り合う貯水槽の下流側の貯水槽が、上流側の貯水槽に連結されている充填層よりも下流の充填層に連結されている。各貯水槽に導入された処理水は、各貯水槽に貯留された後、下流の貯水槽に流れて第3貯水槽103に達する。そして、第3貯水槽103の水は再び充填層に散水され、こうして水は貯水槽と充填層の間を循環する。各貯水槽では、曝気用配管15-1及び15-2により曝気を行い微生物の培養に好適な環境を整えている。また、各貯水槽には、発泡ガラス16を投入し、微生物がより増殖しやすい環境を整えている。 The water in the third water tank 103 is pumped up by the sprinkler pump 71, passes through the sprinkler channel 7, and is sprayed from the sprinkler nozzles 72 and 73 to the packed bed. The sprinkler channel 7 is divided into three on the way, one above the second packing layer 22, the third packing layer 31 and the sixth packing layer 42, and one above the first packing layer 21, the fourth packing layer 32 and Above the fifth filling layer 41 , one leads above the odor gas introduction path 11 . In the deodorizing apparatus of FIG. 1, the water in the third water tank 103, which is the most downstream water tank, is sprinkled over all the packed layers. The water that has passed through the second packed layer 22 and the first packed layer 21 is introduced into the first water tank 101 by dropping down through the buffer chamber S1a (also serving as a treated water passage). Similarly, the water that has passed through the third packed layer 31 and the fourth packed layer 32 is introduced into the second water tank 102 by dropping down through the buffer chamber S2a (which also serves as a treated water passage). The water that has passed through the packed layer 42 and the fifth packed layer 41 is introduced into the third water tank 103 by dropping down through the buffer chamber S3a (which also serves as a treated water passage). In the deodorizing apparatus of FIG. 1, the water (treated water) that has passed through the packed bed is introduced into the water tank upstream of the third water tank 103 serving as the supply source of the water to be sprinkled, and is also introduced into the third water tank 103. have been introduced. In addition, in the third water tank 103 and the water tanks 101 and 102 upstream thereof, the water tank on the downstream side of the adjacent water tanks is connected to the packed bed downstream of the packed bed connected to the upstream water tank. It is After the treated water introduced into each water tank is stored in each water tank, it flows to the downstream water tank and reaches the third water tank 103 . Then, the water in the third water tank 103 is sprinkled on the packed bed again, and thus the water circulates between the water tank and the packed bed. Each water tank is aerated by aeration pipes 15-1 and 15-2 to prepare an environment suitable for culturing microorganisms. In addition, foam glass 16 is put into each water tank to prepare an environment in which microorganisms can grow more easily.

図1の脱臭装置では、第1貯水槽101に導入される処理水が最も栄養分が多く微生物も多くなっている。この処理水が第1貯水槽101に導入されて微生物の培養のサイクルが始まり、第2貯水槽102、第3貯水槽103に移っていくにしたがって安定して培養が進む。一方で、微生物の増殖により栄養分は減っていき、さらに下流の貯水槽にいくにしたがって、導入される処理水中の栄養分も減っていくので、第3貯水槽103には増殖した多くの微生物を含みながら栄養分が少な水が溜まる。この水に含まれる微生物は、いわゆる腹を減らして餌を求めている状態のため、この水を散布すると臭気成分の分解が促進される。図1の脱臭装置では、第2脱臭、第3脱臭、第4脱臭と進むにつれ充填層の容積を小さくしている。これは臭気成分の濃度により対応した脱臭(臭気成分の濃度は、第2脱臭から第4脱臭に進むにつれ小さくなっている)を行うためであるが、第2脱臭~第4脱臭まで同じ容積でもよい。必要に応じて微生物や微生物資材を貯水槽に添加してもよく、この添加は自動でも手動でもよい。 In the deodorizing apparatus of FIG. 1, the treated water introduced into the first water tank 101 contains the most nutrients and the most microorganisms. This treated water is introduced into the first water tank 101 to start the cycle of culturing microorganisms, and as it moves to the second water tank 102 and the third water tank 103, the culture progresses stably. On the other hand, the growth of microorganisms reduces the nutrients, and the nutrients in the treated water introduced also decrease as it goes to the downstream water storage tanks, so the third water storage tank 103 contains many multiplied microorganisms. However, there is little nutrients and water accumulates. Microorganisms contained in this water are in a so-called hunger-seeking state in which they seek food. In the deodorizing apparatus of FIG. 1, the volume of the packed bed is reduced as the second, third, and fourth deodorizing steps progress. This is because the deodorization corresponding to the concentration of the odor component (the concentration of the odor component decreases from the second deodorization to the fourth deodorization) is performed. good. Microorganisms or microbial materials may be added to the reservoir as desired, and this addition may be automatic or manual.

本発明の他の一実施形態を、図2を用いて説明する。臭気ガスは、臭気ガス導入路11を通って第1充填層B1に導入される。導入された臭気ガスは、第1充填層B1を通過し、第2充填層B2、第3充填層C2、第4充填層C1、第5充填層D1、第6充填層D2、第7充填層E2、第8充填層E1、第9充填層F1、第10充填層F2と下流の充填層を順に通過して、臭気ガス排出路12から排出される。各充填層の間には、図1の脱臭装置と同様に緩衝室が設けられている。一方で、水供給路13から第1貯水槽101に水が供給され、供給された水は水通路13-1を通って第2貯水槽102に流れ、第2貯水槽102の水は水通路13-2を通って第3貯水槽103に流れ、第3貯水槽103の水は水通路13-3を通って第4貯水槽104に流れ、第4貯水槽104の水は水通路13-4を通って第5貯水槽105に流れる。水通路13-1と13-3では、貯水槽と貯水槽の間の壁に水が通過する穴があけられており、水通路13-2と13-4では、図1の脱臭装置と同様にオーバーフローにより水が移動している。 Another embodiment of the present invention will be described with reference to FIG. The odorous gas is introduced into the first filling layer B1 through the odorous gas introduction path 11 . The introduced odorous gas passes through the first packing layer B1, the second packing layer B2, the third packing layer C2, the fourth packing layer C1, the fifth packing layer D1, the sixth packing layer D2, and the seventh packing layer. E2, the eighth packed layer E1, the ninth packed layer F1, the tenth packed layer F2, and the downstream packed layers in this order are discharged from the odorous gas discharge path 12. FIG. Buffer chambers are provided between the packed layers as in the deodorizing apparatus of FIG. On the other hand, water is supplied from the water supply path 13 to the first water tank 101, the supplied water flows through the water passage 13-1 to the second water tank 102, and the water in the second water tank 102 flows through the water passage. 13-2 to the third water tank 103, the water in the third water tank 103 flows to the fourth water tank 104 through the water passage 13-3, and the water in the fourth water tank 104 flows to the water passage 13- 4 into the fifth water tank 105 . In the water passages 13-1 and 13-3, the walls between the water tanks are provided with holes through which water passes. water is moving due to overflow.

第1貯水槽101の水は、散水路7-3を通って、第6充填層D2及び第5充填層D1に散水される。第2貯水槽102の水は、散水路7-2を通って、第3充填層C2及び第4充填層C1に散水される。第3貯水槽103の水は、散水路7-1を通って、第2充填層B2及び第1充填層B1に散水される。散水路7-1、7-2及び7-3は途中で二つに分かれ、一方はそれぞれ第2充填層B2、第3充填層C2及び第6充填層D2の上方に、他方はそれぞれ第1充填層B1、第4充填層C1及び第5充填層D1の上方に通じている。また、第5貯水槽105の水は、散水路7-4を通って、第7充填層E2、第8充填層E1、第10充填層F2及び第9充填層F1に散水される。散水路7-4は途中で3つに分かれ、1つは第7充填層E2及び第10充填層F2の上方に、1つは第8充填層E1及び第9充填層F1の上方に、1つは臭気ガス導入路11に通じている。第2充填層B2及び第1充填層B1に散水された水は、各充填層を通過して第1貯水槽101に落下することにより導入される。同様に、第3充填層C2及び第4充填層C1に散水された水、第6充填層D2及び第5充填層D1に散水された水、第7充填層E2及び第8充填層E1に散水された水、第10充填層F2及び第9充填層F1に散水された水は、それぞれ第2貯水槽102、第3貯水槽103、第4貯水槽104、第5貯水槽105に落下して導入される。 The water in the first water tank 101 is sprinkled on the sixth packed bed D2 and the fifth packed bed D1 through the sprinkler channel 7-3. The water in the second water tank 102 is sprinkled on the third packed layer C2 and the fourth packed layer C1 through the sprinkler channel 7-2. The water in the third water tank 103 is sprinkled on the second packed bed B2 and the first packed bed B1 through the sprinkler channel 7-1. The sprinkler channels 7-1, 7-2 and 7-3 are divided into two on the way, one above the second packing layer B2, the third packing layer C2 and the sixth packing layer D2 respectively, and the other above the first packing layer D2 respectively. It communicates above the filling layer B1, the fourth filling layer C1 and the fifth filling layer D1. Also, the water in the fifth water tank 105 is sprinkled through the sprinkler channel 7-4 to the seventh packed layer E2, the eighth packed layer E1, the tenth packed layer F2 and the ninth packed layer F1. The sprinkler channel 7-4 is divided into three along the way, one above the seventh and tenth packing layers E2 and F2, one above the eighth and ninth packing layers E1 and F1, and one above the eighth and ninth packing layers E1 and F1. One is connected to the odor gas introduction path 11 . The water sprinkled on the second packed bed B2 and the first packed bed B1 is introduced by passing through each packed bed and dropping into the first water tank 101 . Similarly, the water sprinkled on the third packed layer C2 and the fourth packed layer C1, the water sprinkled on the sixth packed layer D2 and the fifth packed layer D1, the seventh packed layer E2 and the eighth packed layer E1. The water sprinkled on the tenth packed layer F2 and the water sprinkled on the ninth packed layer F1 drop into the second water tank 102, the third water tank 103, the fourth water tank 104, and the fifth water tank 105, respectively. be introduced.

第3貯水槽103の水は、第3貯水槽103が連結している第6充填層D2及び第5充填層D1よりも上流の第2充填層B2及び第1充填層B1に散水され、第1貯水槽101の水は、第1貯水槽101が連結している第2充填層B2及び第1充填層B1よりも下流の第6充填層D2及び第5充填層D1に散水され、第2貯水槽102の水は、第2貯水槽102が連結している第3充填層C2及び第4充填層C1に散水される。このため、第1貯水槽101~第3貯水槽103の中で最も臭気成分の分解能力の高い水を、最も臭気成分の多い(負荷の高い)充填層に散水し、最も臭気成分の分解能力の低い水を、最も臭気成分の少ない(負荷の低い)充填層に散水することができるので、負荷を均一化し分解処理の効率化を図ることができる。また、第7充填層E2から下流の充填層に流れる臭気ガスは、脱臭がある程度進み臭気成分が少なくなっている。そのため、第4貯水槽104及び第5貯水槽105に導入される処理水中の栄養分及び微生物はそれほど多くなくいが、臭気成分の少ない第7充填層E2~第10充填層F2には、第5貯水槽105の水を散水することにより十分に臭気成分を分解することができる。 The water in the third water tank 103 is sprinkled on the second packed bed B2 and the first packed bed B1 upstream of the sixth packed bed D2 and the fifth packed bed D1 to which the third water tank 103 is connected. The water in the first water tank 101 is sprinkled on the sixth packed layer D2 and the fifth packed layer D1 downstream of the second packed layer B2 and the first packed layer B1 to which the first water tank 101 is connected. The water in the water tank 102 is sprinkled on the third packed layer C2 and the fourth packed layer C1 to which the second water tank 102 is connected. For this reason, the water having the highest ability to decompose odorous components in the first water tank 101 to the third water tank 103 is sprinkled over the packed bed with the highest amount of odorous components (highest load), and the water having the highest ability to decompose odorous components. Since the water with the lowest odor component can be sprinkled on the packed bed with the least odor component (lowest load), the load can be made uniform and the efficiency of the decomposition treatment can be improved. In addition, the odorous gas flowing from the seventh packed layer E2 to the downstream packed layer has been deodorized to some extent and has less odorous components. Therefore, although the amount of nutrients and microorganisms in the treated water introduced into the fourth water tank 104 and the fifth water tank 105 is not so large, the seventh to tenth packed layers E2 to F2, which contain few odorous components, contain the fifth By sprinkling the water in the water tank 105, the odorous components can be sufficiently decomposed.

図1のタイプの脱臭装置(ただし、第2脱臭~第4脱臭までの充填層の容積は同じ)を使用して脱臭を行った。脱臭装置の大きさは、幅1100mm×奥行600mm×高さ1400mmであり、脱臭装置内の充填層の容量は合計で0.60m、充填材としてpH7の発泡ガラスを使用した。この脱臭装置に43mの養豚コンポストからの臭気ガスを、40℃まで冷却して、流量1.5m/分で導入した。各充填層への散水量は、それぞれ0.0042m/分であった。各貯水槽中の水の量は、それぞれ約0.1mであった。各貯水槽には、それぞれ約0.03mの発泡ガラスを投入した。各貯水槽の水には、マイクロバブル発生機により空気を送り込んだ。その結果を表1に示す。発酵過程であるコンポスト運転時のコンポストからの排気の臭気濃度(アンモニア濃度)は1000ppm以上であったが(測定器の検出範囲を超えたため、それ以上の濃度は測定できなかった)、脱臭装置からの排気の臭気濃度は20ppmと極めて低い値にまで減少した。また、コンポスト発酵完了時のコンポストからの排気の臭気濃度は300ppmであったが、脱臭装置からの排気の臭気濃度は15ppmと極めて低い値にまで減少した。このように、本発明の脱臭装置は、臭気濃度の広い範囲にわたり、臭気濃度に応じて適切な脱臭処理が行え、非常にコンパクトでありながら、優れた脱臭効果を有した。本脱臭装置は、同等の能力の従来の装置に比べて1/5~1/50程度の大きさであった。 Deodorization was carried out using the deodorizing apparatus of the type shown in FIG. The size of the deodorizing device was 1100 mm wide×600 mm deep×1400 mm high, the total capacity of the filling layer in the deodorizing device was 0.60 m 3 , and pH 7 foam glass was used as the filling material. 43 m 3 of malodorous gas from swine compost was cooled to 40° C. and introduced into this deodorizing apparatus at a flow rate of 1.5 m 3 /min. The amount of water sprayed to each packed bed was 0.0042 m 3 /min. The amount of water in each reservoir was about 0.1 m3 respectively. About 0.03 m 3 of foam glass was put into each water tank. Air was sent into the water in each water tank by a microbubble generator. Table 1 shows the results. The odor concentration (ammonia concentration) of the exhaust gas from the compost during the composting operation, which is a fermentation process, was 1000 ppm or more (because it exceeded the detection range of the measuring instrument, it was not possible to measure a concentration higher than that), but from the deodorizing device. The odor concentration of the exhaust gas was reduced to an extremely low value of 20 ppm. Also, the odor concentration in the exhaust air from the compost at the completion of the compost fermentation was 300 ppm, but the odor concentration in the exhaust air from the deodorizer decreased to an extremely low value of 15 ppm. As described above, the deodorizing apparatus of the present invention was able to perform appropriate deodorizing treatment according to the odor concentration over a wide range of odor concentrations, and had an excellent deodorizing effect in spite of being extremely compact. This deodorizing device was about 1/5 to 1/50 the size of a conventional device of equivalent capacity.

Figure 2022160854000002
Figure 2022160854000002

本発明の脱臭装置及び脱臭方法は、各種の脱臭に使用でき、特に養豚、養鶏等の畜産施設からの強烈な悪臭の脱臭に好適に使用でき、コンポストからの悪臭の脱臭にも好適である。また、畜産施設からの悪臭のみでなく、有機物による悪臭であればどのような施設や悪臭源からの臭気ガスに対しても対応可能であり、例えば、排水処理施設、食品工場等からの悪臭の脱臭にも使用できる。 INDUSTRIAL APPLICABILITY The deodorizing apparatus and deodorizing method of the present invention can be used for various deodorizing purposes, particularly suitable for deodorizing strong odors from livestock facilities such as pig farming and poultry farming, and is also suitable for deodorizing compost. In addition to odors from livestock facilities, it is also possible to deal with odorous gases from any facility or odor source as long as it is caused by organic substances. It can also be used for deodorizing.

11 臭気ガス導入路
12 臭気ガス排出路
13 水供給路
13-1 水通路
13-2 水通路
14 水排出路
15-1 曝気用配管
15-2 曝気用配管
16 発泡ガラス
21 第1充填層
22 第2充填層
31 第3充填層
32 第4充填層
41 第5充填層
42 第6充填層
7 散水路
7-1 散水路
7-2 散水路
7-3 散水路
7-4 散水路
71 散水用ポンプ
72 散水ノズル
73 散水ノズル
101 第1貯水槽(A水槽)
102 第2貯水槽(B水槽)
103 第3貯水槽(C水槽)
104 第4貯水槽(D水槽)
105 第5貯水槽(E水槽)
S1a 緩衝室(処理水通路)
S1b 緩衝室(処理水通路)
S1c 緩衝室
S2a 緩衝室(処理水通路)
S2b 緩衝室(処理水通路)
S2c 緩衝室
S3a 緩衝室(処理水通路)
S3b 緩衝室(処理水通路)
S3c 緩衝室
B1 第1充填層
B2 第2充填層
C2 第3充填層
C1 第4充填層
D1 第5充填層
D2 第6充填層
E2 第7充填層
E1 第8充填層
F1 第9充填層
F2 第10充填層
11 Odor gas introduction path 12 Odor gas discharge path 13 Water supply path 13-1 Water path 13-2 Water path 14 Water discharge path 15-1 Aeration pipe 15-2 Aeration pipe 16 Foam glass 21 First packed layer 22 Second 2nd packed layer 31 3rd packed layer 32 4th packed layer 41 5th packed layer 42 6th packed layer 7 sprinkler channel 7-1 sprinkler channel 7-2 sprinkler channel 7-3 sprinkler channel 7-4 sprinkler channel 71 sprinkler pump 72 Water nozzle 73 Water nozzle 101 First water tank (A water tank)
102 second water tank (B water tank)
103 third water tank (C water tank)
104 Fourth water tank (D water tank)
105 5th water tank (E water tank)
S1a buffer chamber (treated water passage)
S1b buffer chamber (treated water passage)
S1c buffer chamber S2a buffer chamber (treated water passage)
S2b buffer chamber (treated water passage)
S2c buffer chamber S3a buffer chamber (treated water passage)
S3b buffer chamber (treated water passage)
S3c buffer chamber B1 1st packing layer B2 2nd packing layer C2 3rd packing layer C1 4th packing layer D1 5th packing layer D2 6th packing layer E2 7th packing layer E1 8th packing layer F1 9th packing layer F2 No. 10 packed layers

Claims (12)

臭気ガスを通過させ脱臭するための複数の充填層、微生物を培養するための複数の貯水槽及び前記充填層に前記貯水槽の水を散水するための散水機構を備えた脱臭装置であって、
前記充填層には、微生物を担持した充填材が充填され、
前記充填層は、前記臭気ガスが導入される最上流の充填層から前記臭気ガスが排出される最下流の充填層まで、前記臭気ガスが流れるように連結され、
前記貯水槽は、前記脱臭装置の外部より前記水が供給される最上流の貯水槽から最下流の貯水槽まで、前記水が流れるように連結され、
前記散水機構は、前記最上流の貯水槽より下流の少なくとも1つの貯水槽の水を前記充填層に散水する機構であり、
散水する水の供給元となる貯水槽より上流の貯水槽に、充填層を通過した散水された水が導入されるように、前記充填層と前記貯水槽が連結されている脱臭装置。
A deodorizing device comprising: a plurality of filled layers for passing odorous gas and deodorizing; a plurality of water tanks for culturing microorganisms;
The filling layer is filled with a filling material carrying microorganisms,
The packed bed is connected so that the malodorous gas flows from the most upstream packed bed into which the odorous gas is introduced to the most downstream packed bed from which the odorous gas is discharged,
The water tank is connected so that the water flows from the most upstream water tank to which the water is supplied from the outside of the deodorizing device to the most downstream water tank,
The water sprinkling mechanism is a mechanism for sprinkling water in at least one water tank downstream from the most upstream water tank to the filling layer,
A deodorizing device in which the filling layer and the water tank are connected so that the sprinkled water that has passed through the filling layer is introduced into the water tank upstream of the water tank serving as the supply source of the water to be sprinkled.
散水する水の供給元となる貯水槽及び前記貯水槽より上流の貯水槽は、隣り合う貯水槽の下流側の貯水槽が、上流側の貯水槽に連結されている充填層よりも下流の充填層に連結されていることを特徴とする請求項1記載の脱臭装置。 The water tank serving as the supply source of the water to be sprinkled and the water tank upstream of the water tank are arranged such that the water tank on the downstream side of the adjacent water tank is located downstream of the filling layer connected to the water tank on the upstream side. 2. A deodorizing device according to claim 1, characterized in that it is connected to the layer. 散水機構によって、散水する水の供給元となる貯水槽の水が、前記貯水槽と連結している充填層及び該充填層よりも上流の充填層の少なくとも1つに散水されることを特徴とする請求項2記載の脱臭装置。 A water sprinkling mechanism sprinkles water in a water tank serving as a supply source of water to be sprinkled onto at least one of a packed bed connected to the water tank and a packed bed upstream of the packed bed. The deodorizing device according to claim 2. 散水機構によって、貯水槽の水が、さらに前記貯水槽と連結している充填層よりも下流の充填層に散水されることを特徴とする請求項3記載の脱臭装置。 4. The deodorizing device according to claim 3, wherein the water in the water tank is further sprinkled to the filling layer downstream of the filling layer connected to the water tank by the water spraying mechanism. 充填層と充填層の間及び/又は充填層と貯水槽の間に、緩衝室を設けることを特徴とする請求項1~4のいずれか記載の脱臭装置。 A deodorizing device according to any one of claims 1 to 4, characterized in that a buffer chamber is provided between the packed bed and/or between the packed bed and the water tank. 充填材がpH6.5~8.5の発泡ガラスであることを特徴とする請求項1~5のいずれか記載の脱臭装置。 The deodorizing device according to any one of claims 1 to 5, wherein the filler is foamed glass having a pH of 6.5 to 8.5. 最上流の充填層に導入する臭気ガスの温度を45℃以下に冷却する冷却装置を備えることを特徴とする請求項1~6のいずれか記載の脱臭装置。 The deodorizing apparatus according to any one of claims 1 to 6, further comprising a cooling device for cooling the temperature of the odorous gas introduced into the most upstream packed layer to 45°C or less. 少なくとも1つの充填層を内部に有する充填塔が横方向に複数配置され、前記充填塔それぞれの下方に貯水槽が配置され、散水機構により前記充填塔内に散水された水が散水された前記充填塔の下方の貯水槽に、前記充填塔内の前記充填層を通過して導入されるように、前記充填塔と前記貯水槽が配置された請求項1~7のいずれか記載の脱臭装置。
かつ、
A plurality of packed towers having at least one packed bed inside are arranged in the horizontal direction, a water tank is arranged below each of the packed towers, and the packed tower is sprinkled with water sprinkled into the packed tower by a sprinkler mechanism. The deodorizing apparatus according to any one of claims 1 to 7, wherein the packed tower and the water tank are arranged so that the water is introduced into the water tank below the tower through the packed bed in the packed tower.
And,
pHが6.5~8.5である脱臭に用いるための微生物担持用発泡ガラス。 A microorganism-carrying foam glass for deodorizing, having a pH of 6.5 to 8.5. 臭気ガスの脱臭方法であって、
臭気ガスを通過させ脱臭するための微生物を担持した充填材が充填された複数の充填層、微生物を培養するための複数の貯水槽及び前記充填層に前記貯水槽の水を散水するための散水機構を用意し、
前記充填層を、前記臭気ガスが導入される最上流の充填層から前記臭気ガスが排出される最下流の充填層まで、前記臭気ガスが流れるように連結させ、
前記貯水槽を、前記水が供給される最上流の貯水槽から最下流の貯水槽まで、前記水が流れるように連結させ、
前記充填層に臭気ガスを導入し、前記貯水槽に水を供給して、
前記最上流の貯水槽より下流の少なくとも1つの貯水槽の水を前記充填層に散水し、
散水する水の供給元となる貯水槽より上流の貯水槽に、充填層を通過した散水された水を導入する脱臭方法。
A method for deodorizing odorous gas,
A plurality of packed beds filled with a filler supporting microorganisms for passing odorous gas and deodorizing, a plurality of water tanks for culturing the microorganisms, and water sprinkling for spraying the water of the water tanks on the packed beds. prepare the mechanism
connecting the packed bed so that the odorous gas flows from the most upstream packed bed into which the odorous gas is introduced to the most downstream packed bed from which the odorous gas is discharged;
connecting the water tanks so that the water flows from the most upstream water tank to which the water is supplied to the most downstream water tank;
introducing an odorous gas into the packed bed and supplying water to the water tank,
Sprinkling water in at least one water tank downstream from the most upstream water tank to the packed bed,
A deodorizing method of introducing sprinkled water that has passed through a filling layer into a water storage tank upstream of a water storage tank that supplies the water to be sprinkled.
臭気ガスの温度を45℃以下に冷却した後、充填層に前記臭気ガスを導入することを特徴とする請求項10記載の脱臭方法。 11. The deodorizing method according to claim 10, wherein the odorous gas is introduced into the packed bed after the temperature of the malodorous gas is cooled to 45[deg.] C. or less. 微生物資材を貯水槽に導入することを特徴とする請求項10又は11記載の脱臭方法。



12. The deodorizing method according to claim 10, wherein the microbial material is introduced into the water tank.



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