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JP6278796B2 - Deodorization device - Google Patents

Deodorization device Download PDF

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JP6278796B2
JP6278796B2 JP2014074414A JP2014074414A JP6278796B2 JP 6278796 B2 JP6278796 B2 JP 6278796B2 JP 2014074414 A JP2014074414 A JP 2014074414A JP 2014074414 A JP2014074414 A JP 2014074414A JP 6278796 B2 JP6278796 B2 JP 6278796B2
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odor
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JP2015196119A (en
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佐藤 達也
佐藤  達也
剛 安部
剛 安部
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クボタ環境サ−ビス株式会社
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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Description

本発明は、被処理気体を臭気捕捉液中に導入する導入部と、前記被処理気体と前記臭気捕捉液との気液混合が行われて前記被処理気体中の臭気が除去される気液混合部とを備える、所謂スクラバー方式の脱臭装置に関する。   The present invention provides a gas / liquid in which an odor in the gas to be treated is removed by mixing the gas to be treated with the gas to be treated and the odor trapping liquid by introducing the gas to be treated into the odor trapping liquid. The present invention relates to a so-called scrubber type deodorizing apparatus including a mixing unit.

従来のスクラバー式脱臭装置では、例えば特許文献1に示すように、臭気捕捉液を供給するための液体供給口が導入部の側面に設けられているものが多い。   In conventional scrubber type deodorizing apparatuses, for example, as shown in Patent Document 1, a liquid supply port for supplying an odor trapping liquid is often provided on a side surface of an introduction portion.

実用新案登録第3132698号(図1)Utility Model Registration No. 3132698 (Figure 1)

従来の脱臭装置では、臭気捕捉液が導入部の側面から供給されるため、臭気捕捉液が装置内で上下に大きく波打ち、これにより装置内の臭気捕捉液や被処理気体が脈動するような動きをしてしまうことがある。その結果、臭気捕捉液と被処理気体との接触効率が低下して被処理気体中の臭気の除去効率も低下する。また、臭気捕捉液の液面の波打ちを抑制するための整流板などを設置する必要が生じるため装置が複雑化する。
従って本発明の目的は、臭気捕捉液や被処理気体の脈動を抑えたスクラバー式の脱臭装置を提供することにある。
In the conventional deodorizing apparatus, since the odor capturing liquid is supplied from the side surface of the introduction part, the odor capturing liquid undulates up and down in the apparatus, and the movement in which the odor capturing liquid and the gas to be processed in the apparatus pulsate. May end up. As a result, the contact efficiency between the odor trapping liquid and the gas to be processed decreases, and the odor removal efficiency in the gas to be processed also decreases. Moreover, since it becomes necessary to install the baffle plate etc. for suppressing the waviness of the liquid surface of an odor capture | acquisition liquid, an apparatus becomes complicated.
Accordingly, an object of the present invention is to provide a scrubber-type deodorizing device that suppresses the pulsation of the odor trapping liquid and the gas to be treated.

本発明の脱臭装置に係る第1特徴構成は、被処理気体を臭気捕捉液中に導入する導入部と、前記被処理気体と前記臭気捕捉液との気液混合が行われて前記被処理気体中の臭気が除去される気液混合部とを備える脱臭装置において、前記臭気捕捉液を前記導入部に供給するための液体供給口を、前記被処理気体と前記臭気捕捉液との接触面に対向する前記導入部の底壁に設けてあり、前記導入部と前記気液混合部との間に仕切り壁が設けられており、前記仕切り壁の下に前記被処理気体及び前記臭気捕捉液が移動可能な連通口が設けられており、前記臭気捕捉液に導入された前記被処理気体が、前記連通口を通過して前記気液混合部に移動する点にある。 The first characteristic configuration according to the deodorizing apparatus of the present invention is that the gas to be treated is obtained by mixing the gas to be treated with the introduction portion for introducing the gas to be treated into the odor trapping liquid and the gas to be treated and the odor trapping liquid. In a deodorizing apparatus comprising a gas-liquid mixing unit from which odors are removed, a liquid supply port for supplying the odor capturing liquid to the introduction unit is provided on a contact surface between the gas to be treated and the odor capturing liquid. It is provided on the bottom wall of the introduction part facing, a partition wall is provided between the introduction part and the gas-liquid mixing part, and the gas to be treated and the odor trapping liquid are below the partition wall. A movable communication port is provided, and the gas to be treated introduced into the odor capturing liquid passes through the communication port and moves to the gas-liquid mixing unit .

〔作用及び効果〕
本構成によれば、被処理気体と臭気捕捉液との接触面に対向するように導入部の底壁に液体供給口を設けてあるため、被処理気体の圧力と臭気捕捉液の圧力とが互いに打ち消し合って液位が保たれ、臭気捕捉液が装置内で波打ちし難くなる。その結果、装置内の臭気捕捉液や被処理気体が脈動するような動きを防止することができる。
[Action and effect]
According to this configuration, since the liquid supply port is provided in the bottom wall of the introduction portion so as to face the contact surface between the gas to be processed and the odor capturing liquid, the pressure of the gas to be processed and the pressure of the odor capturing liquid are The liquid level is maintained by canceling each other, and the odor trapping liquid becomes difficult to wave in the apparatus. As a result, it is possible to prevent the odor trapping liquid and the gas to be processed in the apparatus from pulsating.

第2特徴構成は、複数の前記導入部及び前記気液混合部を備え、前記被処理気体の前記臭気捕捉液への導入と、前記被処理気体と前記臭気捕捉液との気液混合が交互に行われるように構成されており、前記被処理気体が前記臭気捕捉液中に最初に導入される導入部の底壁にのみ前記液体供給口を設けてある点にある。   The second characteristic configuration includes a plurality of the introduction units and the gas-liquid mixing unit, and the introduction of the gas to be processed into the odor capturing liquid and the gas-liquid mixing of the gas to be processed and the odor capturing liquid are alternately performed. The liquid supply port is provided only on the bottom wall of the introduction part where the gas to be treated is first introduced into the odor trapping liquid.

〔作用及び効果〕
本構成によれば、複数の導入部及び気液混合部を備えるため、被処理気体中の臭気をより効率的に除去することができる。また、被処理気体が初めに導入される導入部における臭気捕捉液や被処理気体の脈動を抑えることによって、その下流に配置されるすべての導入部及び気液混合部における臭気捕捉液や被処理気体の脈動を抑えることができる。従って、本構成のごとく、被処理気体が臭気捕捉液中に最初に導入される導入部の底壁にのみ液体供給口を設けておけば、下流に配置される導入部の底壁に液体供給口を設ける必要がなく装置構成が簡素なものとなる。
[Action and effect]
According to this configuration, since a plurality of introduction parts and gas-liquid mixing parts are provided, the odor in the gas to be treated can be more efficiently removed. In addition, by suppressing the odor capturing liquid and the pulsation of the gas to be treated in the introduction part where the gas to be treated is first introduced, the odor capturing liquid and the liquid to be treated in all the introducing parts and gas-liquid mixing parts arranged downstream thereof Gas pulsation can be suppressed. Therefore, as in this configuration, if the liquid supply port is provided only on the bottom wall of the introduction portion where the gas to be treated is first introduced into the odor trapping liquid, the liquid supply is supplied to the bottom wall of the introduction portion disposed downstream. It is not necessary to provide a mouth, and the device configuration is simplified.

第3特徴構成は、下流側に位置する仕切り壁の下端が、上流側に位置する仕切り壁の下端よりも高い位置に設定されており、下流側の連通口が上流側の連通口よりも大きくなるように設定されている点にある。 The third characteristic configuration, the lower end of the partition wall located on the lower stream side, is set at a higher position than the lower end of the partition wall located upstream, than the communication port of the communication port of the downstream side upstream It is in the point set so that it may become large.

〔作用及び効果〕
本構成によれば、下流側の気液混合部での気液混合の効率を維持することができる。
[Action and effect]
According to this configuration, the efficiency of gas-liquid mixing in the gas-liquid mixing unit on the downstream side can be maintained.

第4特徴構成は、前記被処理気体が、さらに粉塵を含む点にある。   A fourth characteristic configuration is that the gas to be processed further contains dust.

〔作用及び効果〕
本構成によれば、被処理気体から臭気だけなく粉塵を除去することが可能であり、被処理気体をより清澄化することができる。
[Action and effect]
According to this structure, it is possible to remove not only odor but also dust from the gas to be treated, and the gas to be treated can be further clarified.

第5特徴構成は、前記臭気捕捉液が、汚泥である点にある。   The fifth characteristic configuration is that the odor trapping liquid is sludge.

〔作用及び効果〕
本構成によれば、臭気捕捉液として汚泥を使用するため、例えば、屎尿処理施設等で使用される活性汚泥を利用することも可能となる。従ってこの場合、臭気捕捉液を別途用意する必要がなく、効率的に脱臭処理を行うことができる。
[Action and effect]
According to this configuration, since sludge is used as the odor capturing liquid, it is possible to use activated sludge used in, for example, a sewage treatment facility. Therefore, in this case, it is not necessary to separately prepare an odor capturing liquid, and the deodorizing process can be performed efficiently.

脱臭装置の断面図である。It is sectional drawing of a deodorizing apparatus. 脱臭装置を備える屎尿処理設備の概略を示す構成図である。It is a block diagram which shows the outline of the manure processing equipment provided with a deodorizing apparatus. 脱臭装置を備える別の屎尿処理設備の概略を示す構成図である。It is a block diagram which shows the outline of another manure processing equipment provided with a deodorizing apparatus. 脱臭装置を備える別の屎尿処理設備の概略を示す構成図である。It is a block diagram which shows the outline of another manure processing equipment provided with a deodorizing apparatus. 脱臭装置を備える別の屎尿処理設備の概略を示す構成図である。It is a block diagram which shows the outline of another manure processing equipment provided with a deodorizing apparatus.

以下、本発明の実施形態について、図面に基づいて説明する。
〔脱臭装置〕
図1に示すように、本実施形態における脱臭装置1は、所謂スクラバー方式の脱臭装置であって、上壁2、左側壁3、段部を形成する右側壁4、底壁5、表壁(図示せず)及び裏壁(図示せず)を備えて構成される。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[Deodorization equipment]
As shown in FIG. 1, a deodorizing apparatus 1 according to this embodiment is a so-called scrubber type deodorizing apparatus, and includes an upper wall 2, a left side wall 3, a right side wall 4 forming a stepped portion, a bottom wall 5, a front wall ( (Not shown) and a back wall (not shown).

上壁2には、被処理気体Gを供給するための気体供給口6と、被処理気体Gを排出するための気体排出口7とを設けてある。底壁5には、臭気捕捉液Lを供給するための液体供給口8と、臭気捕捉液Lを排出するための液体排出口9と、ドレインバルブを備える液体排出機構10とを設けてある。   The upper wall 2 is provided with a gas supply port 6 for supplying the gas G to be processed and a gas outlet 7 for discharging the gas G to be processed. The bottom wall 5 is provided with a liquid supply port 8 for supplying the odor capture liquid L, a liquid discharge port 9 for discharging the odor capture liquid L, and a liquid discharge mechanism 10 including a drain valve.

脱臭装置1の中には、垂直方向に沿う第1〜第4仕切り壁11〜14、水平方向に対してわずかに傾斜する第5仕切り壁15、及び底壁5から垂直に起立する堰16が設けられている。   In the deodorizing apparatus 1, there are first to fourth partition walls 11 to 14 along the vertical direction, a fifth partition wall 15 slightly inclined with respect to the horizontal direction, and a weir 16 standing upright from the bottom wall 5. Is provided.

尚、第4仕切り壁14は、後述する第2気液混合部33と液体排出部35との間に設けられており、液体排出部35における臭気捕捉液Lの上部空間と第2気液混合部33とを遮断する。第5仕切り壁15は、第2仕切り壁12及び第3仕切り壁13の上方に設けられており、第1仕切り壁11の上部から下方に傾斜する傾斜面を形成する。   In addition, the 4th partition wall 14 is provided between the 2nd gas-liquid mixing part 33 and the liquid discharge part 35 which are mentioned later, The upper space of the odor capture liquid L in the liquid discharge part 35, and 2nd gas-liquid mixing The part 33 is shut off. The fifth partition wall 15 is provided above the second partition wall 12 and the third partition wall 13, and forms an inclined surface that inclines downward from the upper part of the first partition wall 11.

第1〜第4仕切り壁11〜14のそれぞれの下端と底壁5との間に第1〜第4連通口21〜24が形成される。第2仕切り壁12の上端と第5仕切り壁15との間に第5連通口25が形成される。第5仕切り壁15の下端と右側壁4との間に第6連通口26が形成される。   First to fourth communication ports 21 to 24 are formed between the lower ends of the first to fourth partition walls 11 to 14 and the bottom wall 5. A fifth communication port 25 is formed between the upper end of the second partition wall 12 and the fifth partition wall 15. A sixth communication port 26 is formed between the lower end of the fifth partition wall 15 and the right side wall 4.

尚、本実施形態においては、第1仕切り壁11の下端は、第3仕切り壁13の下端よりも低い位置に設定されており、堰16の高さは、第3仕切り壁13の下端と略同じ高さに設定されている。   In the present embodiment, the lower end of the first partition wall 11 is set at a position lower than the lower end of the third partition wall 13, and the height of the weir 16 is substantially the same as the lower end of the third partition wall 13. It is set to the same height.

脱臭装置1内の空間は、上述の第1〜第5仕切り壁11〜15によって仕切られることによって、第1導入部30、第1気液混合部31、第2導入部32、第2気液混合部33、気液分離部34、及び液体排出部35が形成されている。尚、液体排出部35は、右側壁4の段部の内側に形成されている。   The space in the deodorizing apparatus 1 is partitioned by the first to fifth partition walls 11 to 15 described above, so that the first introduction part 30, the first gas-liquid mixing part 31, the second introduction part 32, and the second gas-liquid are separated. A mixing unit 33, a gas-liquid separation unit 34, and a liquid discharge unit 35 are formed. The liquid discharge portion 35 is formed inside the step portion of the right side wall 4.

第1臭気除去部は、第1導入部30と第1気液混合部31から構成されるものであり、第2臭気除去部は、第2導入部32と第2気液混合部33から構成されるものと定義する。   The first odor removing unit is configured by the first introduction unit 30 and the first gas / liquid mixing unit 31, and the second odor removal unit is configured by the second introduction unit 32 and the second gas / liquid mixing unit 33. Defined as

第1導入部30における上壁2の部分及び底壁5の部分のそれぞれには、気体供給口6及び液体供給口8が互いに対向するように設けられている。液体排出機構10は第2気液混合部33の底壁5の部分に設けられている。気体排出口7は、被処理気体Gの移動距離を稼ぐため、気液分離部34の上壁2の部分の第1仕切り壁11に近い位置、即ち第6連通口26から最も遠い位置に設けられている。堰16は液体排出部35の底壁5の部分に立設し、その堰16と右側壁4との間の底壁5の部分に液体排出口9が設けられている。   A gas supply port 6 and a liquid supply port 8 are provided in each of the upper wall 2 portion and the bottom wall 5 portion of the first introduction portion 30 so as to face each other. The liquid discharge mechanism 10 is provided on the bottom wall 5 of the second gas-liquid mixing unit 33. The gas discharge port 7 is provided at a position close to the first partition wall 11 of the upper wall 2 of the gas-liquid separator 34, that is, a position farthest from the sixth communication port 26 in order to increase the moving distance of the gas G to be processed. It has been. The weir 16 is erected on the bottom wall 5 of the liquid discharge portion 35, and the liquid discharge port 9 is provided on the bottom wall 5 between the weir 16 and the right side wall 4.

第1連通口21を介して第1導入部30と第1気液混合部31とが連通する。第2連通口22及び第5連通口25を介して第1気液混合部31と第2導入部32とが連通する。第3連通口23を介して第2導入部32と第2気液混合部33とが連通する。尚、第1連通口21が第3連通口23よりも小さくなるように設定されている。第4連通口24を介して第2気液混合部33と液体排出部35とが連通する。第5連通口25を介して第2気液混合部33と気液分離部34とが連通する。   The first introduction part 30 and the first gas-liquid mixing part 31 communicate with each other through the first communication port 21. The first gas-liquid mixing unit 31 and the second introduction unit 32 communicate with each other through the second communication port 22 and the fifth communication port 25. The second introduction part 32 and the second gas-liquid mixing part 33 communicate with each other through the third communication port 23. The first communication port 21 is set to be smaller than the third communication port 23. The second gas / liquid mixing unit 33 and the liquid discharge unit 35 communicate with each other through the fourth communication port 24. The second gas / liquid mixing unit 33 and the gas / liquid separation unit 34 communicate with each other through the fifth communication port 25.

図1中の点線の矢印に示すように、気体供給口6から第1導入部30に供給された被処理気体Gは、第1連通口21、第1気液混合部31、第5連通口25、第2導入部32、第3連通口23、第2気液混合部33、第6連通口26、及び気液分離部34へと順次流れ、気体排出口7から排出される。   As shown by the dotted arrows in FIG. 1, the gas to be processed G supplied from the gas supply port 6 to the first introduction unit 30 is composed of the first communication port 21, the first gas-liquid mixing unit 31, and the fifth communication port. 25, the second introduction part 32, the third communication port 23, the second gas-liquid mixing unit 33, the sixth communication port 26, and the gas-liquid separation unit 34 are sequentially flowed and discharged from the gas discharge port 7.

また、図1中の白抜きの矢印に示すように、液体供給口8から第1導入部30に供給された臭気捕捉液Lは、第1連通口21、第1気液混合部31、第2連通口22、第2導入部32、第3連通口23、第2気液混合部33、第4連通口24、及び液体排出部35へと順次流れ、液体排出口9から排出される。   Moreover, as shown by the white arrow in FIG. 1, the odor trapping liquid L supplied from the liquid supply port 8 to the first introduction unit 30 is the first communication port 21, the first gas-liquid mixing unit 31, The two communication ports 22, the second introduction unit 32, the third communication port 23, the second gas-liquid mixing unit 33, the fourth communication port 24, and the liquid discharge unit 35 are sequentially flowed and discharged from the liquid discharge port 9.

即ち、本実施形態の脱臭装置1においては、被処理気体Gの流路と臭気捕捉液Lの流路とが互いに一部重複しているため、被処理気体Gと臭気捕捉液Lとを同時に供給することによって、被処理気体Gと臭気捕捉液Lとが互いに接触し、これにより被処理気体G中の臭気或いは臭気と粉塵が臭気捕捉液Lに捕捉されて除去される。   That is, in the deodorizing apparatus 1 of this embodiment, the flow path of the gas to be processed G and the flow path of the odor trapping liquid L partially overlap each other. By supplying, the to-be-processed gas G and the odor capturing liquid L come into contact with each other, whereby the odor or odor and dust in the to-be-processed gas G are captured by the odor capturing liquid L and removed.

以下、第1導入部30、第1気液混合部31、第2導入部32、第2気液混合部33、気液分離部34、及び液体排出部35のそれぞれにおける作用及び効果について具体的に述べる。   Hereinafter, the operation and effect of each of the first introduction unit 30, the first gas-liquid mixing unit 31, the second introduction unit 32, the second gas-liquid mixing unit 33, the gas-liquid separation unit 34, and the liquid discharge unit 35 will be described in detail. In the following.

被処理気体Gが気体供給口6から所定の圧力をもって第1導入部30に供給されると共に、臭気捕捉液Lが液体供給口8から所定の圧力をもって第1導入部30に供給(圧入)される。そして、被処理気体Gが、臭気捕捉液Lとの面接触によって臭気捕捉液L中に導入される。   The gas G to be treated is supplied from the gas supply port 6 to the first introduction unit 30 with a predetermined pressure, and the odor capturing liquid L is supplied (press-fit) from the liquid supply port 8 to the first introduction unit 30 with a predetermined pressure. The And the to-be-processed gas G is introduce | transduced in the odor capture | acquisition liquid L by surface contact with the odor capture | acquisition liquid L. FIG.

このとき、液体供給口8が、被処理気体Gと臭気捕捉液Lとの接触面Sに対向するように第1導入部30の底壁5に設けてあるため、被処理気体Gの圧力と臭気捕捉液Lの圧力とが互いに打ち消し合って臭気捕捉液Lが装置内で波打ちし難くなり液位が保たれる。これにより装置内の臭気捕捉液Lや被処理気体Gが脈動するような動きを防止することができる。   At this time, since the liquid supply port 8 is provided on the bottom wall 5 of the first introduction unit 30 so as to face the contact surface S between the gas to be processed G and the odor trapping liquid L, the pressure of the gas to be processed G The pressure of the odor trapping liquid L cancels each other, and the odor trapping liquid L becomes difficult to wave in the apparatus, and the liquid level is maintained. Thereby, the movement which the odor capture | acquisition liquid L in the apparatus and the to-be-processed gas G pulsate can be prevented.

臭気捕捉液Lに導入された被処理気体Gは、第1連通口21を通過して第1気液混合部31に入り、臭気捕捉液Lをまきあげながら第1気液混合部31の上部空間に移動する。このとき、臭気捕捉液Lが多数の細かな粒として一緒にまきあげられることによって、被処理気体Gと臭気捕捉液Lの粒との気液混合が行われる。これにより被処理気体Gと臭気捕捉液Lとが効率良く接触するため、被処理気体G中の臭気或いは臭気と粉塵が臭気捕捉液Lに捕捉されて除去される。   The to-be-processed gas G introduced into the odor trapping liquid L passes through the first communication port 21 and enters the first gas-liquid mixing section 31, and the upper space of the first gas-liquid mixing section 31 while raising the odor trapping liquid L. Move to. At this time, the odor trapping liquid L is sprinkled together as a large number of fine particles, whereby gas-liquid mixing of the gas to be processed G and the odor trapping liquid L particles is performed. As a result, the gas to be treated G and the odor trapping liquid L come into contact with each other efficiently, so that the odor or odor and dust in the gas to be treated G are captured and removed by the odor trapping liquid L.

次いで、第1気液混合部31の上部空間に移動した被処理気体Gは、第5連通口25を通過して第2導入部32に移動し、再び臭気捕捉液Lとの面接触によって臭気捕捉液L中に導入される。   Subsequently, the to-be-processed gas G which moved to the upper space of the 1st gas-liquid mixing part 31 passes the 5th communicating port 25, moves to the 2nd introducing | transducing part 32, and again becomes odor by surface contact with the odor capture liquid L It is introduced into the capture liquid L.

臭気捕捉液Lに導入された被処理気体Gは、第3連通口23を通過して第2気液混合部33に入り、臭気捕捉液Lをまきあげながら第2気液混合部33の上部空間に移動する。このとき第1気液混合部31における場合と同様に、被処理気体Gと臭気捕捉液Lの粒との気液混合が行われ、被処理気体G中の臭気が臭気捕捉液Lに捕捉されて除去される。   The to-be-processed gas G introduced into the odor trapping liquid L passes through the third communication port 23 and enters the second gas-liquid mixing section 33, and the upper space of the second gas-liquid mixing section 33 while raising the odor trapping liquid L. Move to. At this time, similarly to the case of the first gas-liquid mixing unit 31, gas-liquid mixing of the gas to be processed G and the particles of the odor capturing liquid L is performed, and the odor in the gas to be processed G is captured by the odor capturing liquid L. Removed.

次いで、第2気液混合部33の上部空間に移動した被処理気体Gは、第6連通口26を通過して気液分離部34に移動する。気液分離部34は、第2気液混合部33の上方に通じる比較的広い空間を形成する部分である。当該被処理気体Gは臭気捕捉液Lの非常に細かな粒(ミスト)を含むため、被処理気体Gが気液分離部34に入ることによってその流速が低下して臭気捕捉液Lとの分離が促される。分離された臭気捕捉液Lは第5仕切り壁15の傾斜面を伝って第2気液混合部33に流下し回収される。被処理気体Gは、気体排出口7から装置外部に排出される。   Next, the gas to be processed G that has moved to the upper space of the second gas-liquid mixing unit 33 passes through the sixth communication port 26 and moves to the gas-liquid separation unit 34. The gas-liquid separation unit 34 is a part that forms a relatively wide space that communicates above the second gas-liquid mixing unit 33. Since the gas to be treated G contains very fine particles (mist) of the odor trapping liquid L, the flow rate of the gas to be treated G entering the gas-liquid separation unit 34 is reduced and the gas is separated from the odor trapping liquid L. Is prompted. The separated odor capturing liquid L flows along the inclined surface of the fifth partition wall 15 and flows down to the second gas / liquid mixing part 33 and is collected. The gas to be processed G is discharged from the gas discharge port 7 to the outside of the apparatus.

液体供給口8から供給された臭気捕捉液Lは、第1導入部30、第1気液混合部31、第2導入部32、及び第2気液混合部33を順次通過し、被処理気体Gの導入と気液混合とを繰り返しながら、被処理気体G中の臭気を捕捉する。そして、液体排出部35に到達した臭気捕捉液Lは、堰16をオーバーフローによって略垂直に流下し、泡が叩かれて消泡されて液体排出口9から装置外部に排出される。   The odor trapping liquid L supplied from the liquid supply port 8 sequentially passes through the first introduction unit 30, the first gas-liquid mixing unit 31, the second introduction unit 32, and the second gas-liquid mixing unit 33, and the gas to be processed While repeating the introduction of G and gas-liquid mixing, the odor in the gas to be treated G is captured. Then, the odor trapping liquid L that has reached the liquid discharge portion 35 flows down the weir 16 substantially vertically by overflow, is blown by bubbles, is defoamed, and is discharged from the liquid discharge port 9 to the outside of the apparatus.

液体排出部35では、第1導入部、第1気液混合部、第2導入部、及び第2気液混合部において臭気捕捉液Lに導入された気泡が放出されることにより泡が発生し易い。その結果、この泡が気体排出口7付近に溜まることで、被処理気体Gが排出され難くなる場合がある。しかしながら、本実施形態では、液体排出部35で発生した泡が第4仕切り壁14に遮られて第2気液混合部33に移動することができないため、泡が気体排出口7付近に溜まることはない。そのため、被処理気体Gは、泡に邪魔されることなく気体排出口7より排出される。尚、液体排出部35で発生した泡は、堰16をオーバーフローで流下する臭気捕捉液Lと共に液体排出口9から装置外部に排出される。即ち、発生した泡が臭気捕捉液Lの流れに引き込まれるようにして排出されるため、液体排出部35に留まることもない。さらに粉塵が留まることも防止される。   In the liquid discharge unit 35, bubbles are generated by releasing the bubbles introduced into the odor trapping liquid L in the first introduction unit, the first gas-liquid mixing unit, the second introduction unit, and the second gas-liquid mixing unit. easy. As a result, the gas to be processed G may be difficult to be discharged due to the bubbles remaining in the vicinity of the gas discharge port 7. However, in the present embodiment, bubbles generated in the liquid discharge part 35 are blocked by the fourth partition wall 14 and cannot move to the second gas-liquid mixing part 33, so that the bubbles accumulate in the vicinity of the gas discharge port 7. There is no. Therefore, the to-be-processed gas G is discharged | emitted from the gas discharge port 7, without being disturbed by a bubble. The bubbles generated in the liquid discharge unit 35 are discharged from the liquid discharge port 9 to the outside of the apparatus together with the odor capturing liquid L flowing down the weir 16 due to overflow. That is, since the generated bubbles are discharged while being drawn into the flow of the odor trapping liquid L, they do not stay in the liquid discharge portion 35. Further, dust is prevented from staying.

〔被処理気体〕
上述の脱臭装置1に適用可能な被処理気体Gは、少なくとも臭気(例えば、堆肥を作る際に発生するコンポスト臭気や、アンモニアや硫化水素等を含む屎尿臭気等)を含むものであるが、臭気の他にさらに粉塵を(例えば、コンポストの粉塵)含むものであっても良い。
[Processed gas]
The to-be-processed gas G applicable to the above-mentioned deodorizing apparatus 1 contains at least odor (for example, compost odor generated when compost is produced, manure odor containing ammonia, hydrogen sulfide, etc.). Further, it may contain dust (for example, compost dust).

〔臭気捕捉液〕
上述の脱臭装置1に適用可能な臭気捕捉液Lとしては、例えば、水、活性汚泥等の汚泥、硝化液などを挙げることができるが、これらに限定されるものではない。
[Odor capturing liquid]
Examples of the odor capturing liquid L applicable to the above-described deodorizing apparatus 1 include water, sludge such as activated sludge, and nitrification liquid, but are not limited thereto.

〔浄化システム〕
次いで、上述の脱臭装置1を、浄化システムの一例としての屎尿処理設備に組み込んだ形態について説明する。
[Purification system]
Next, an embodiment in which the above-described deodorizing apparatus 1 is incorporated in a manure processing facility as an example of a purification system will be described.

屎尿処理設備では、被処理物である屎尿・浄化槽汚泥について、受入・前処理工程、一次浄化処理工程、二次浄化処理工程、高次処理工程、及び脱臭工程などが実施される。   In the sewage treatment facility, a receiving / pretreatment process, a primary purification process, a secondary purification process, a high-order treatment process, a deodorization process, and the like are performed on the sewage / septic tank sludge to be processed.

図2に示す屎尿処理設備では、受入・前処理工程において、受入槽40、貯留槽41、予備貯留槽42、及び前処理設備43等が使用される。一次浄化処理工程において、深層反応槽44、第1膜原水槽45、第2膜原水槽46、膜原水槽47(又は沈殿槽)、及び返送汚泥槽48等が使用される。二次浄化処理工程において、凝集混和槽49、及び凝集膜原水槽50(又は凝集沈殿槽)等が使用される。高次処理工程において、濾過器・活性炭吸着塔・オゾン接触槽・消毒槽等を備える高度処理設備51が使用される。脱臭工程において、脱臭装置1、中濃度脱臭塔52、及び活性炭吸着塔53等が使用される。尚、図2において実線で示される矢印は、屎尿・浄化槽汚泥の流れを示しており、破線で示される矢印は、臭気を含む空気又は臭気の他に粉塵をも含む空気の流れを示している。   In the manure processing facility shown in FIG. 2, a receiving tank 40, a storage tank 41, a preliminary storage tank 42, a pretreatment facility 43, and the like are used in the reception / pretreatment process. In the primary purification treatment step, a deep reaction tank 44, a first membrane raw water tank 45, a second membrane raw water tank 46, a membrane raw water tank 47 (or a precipitation tank), a return sludge tank 48, and the like are used. In the secondary purification treatment step, an agglomeration mixing tank 49, an agglomerated membrane raw water tank 50 (or an agglomeration sedimentation tank), and the like are used. In the high-order treatment process, an advanced treatment facility 51 including a filter, an activated carbon adsorption tower, an ozone contact tank, a disinfection tank, and the like is used. In the deodorization step, the deodorization apparatus 1, the medium concentration deodorization tower 52, the activated carbon adsorption tower 53, and the like are used. In addition, the arrow shown as a continuous line in FIG. 2 has shown the flow of the manure / septic tank sludge, and the arrow shown by a broken line has shown the flow of the air which also contains dust in addition to odor or odor. .

図2の屎尿処理設備における一次浄化処理工程では活性汚泥処理が実施される。従って、当該屎尿処理設備は、返送汚泥ポンプによって返送汚泥槽48から深層反応槽44に汚泥を返送する返送汚泥ライン54を備えるものであり、上述の脱臭装置1が返送汚泥ライン54中に組み込まれている。尚、屎尿処理設備に既存の返送汚泥ポンプを使用することで、被処理気体と汚泥とを気液混合するための新たなポンプを設置する必要が生じない。   In the primary purification treatment process in the sewage treatment facility of FIG. 2, activated sludge treatment is performed. Therefore, the sewage treatment equipment includes a return sludge line 54 for returning sludge from the return sludge tank 48 to the deep reaction tank 44 by a return sludge pump, and the deodorizing apparatus 1 is incorporated in the return sludge line 54. ing. In addition, it is not necessary to install a new pump for gas-liquid mixing of the gas to be treated and sludge by using the existing return sludge pump in the urine processing equipment.

図2における脱臭装置1では、受入・前処理工程において発生する高濃度臭気を含む空気が被処理気体Gとして供給されると共に、返送汚泥ライン54によって返送される汚泥が臭気捕捉液Lとして供給される。   In the deodorizing apparatus 1 in FIG. 2, air containing a high-concentration odor generated in the receiving / pretreatment process is supplied as the gas to be processed G, and the sludge returned by the return sludge line 54 is supplied as the odor trapping liquid L. The

この構成によれば、被処理気体G中の高濃度臭気が、従来の高濃度脱臭塔によらず、脱臭装置1において汚泥に捕捉されて除去される。そして、高濃度臭気及び粉塵が除去された被処理気体Gが、中濃度脱臭塔52(第2の脱臭装置)に供給されて中濃度臭気が脱臭される。次いで、中濃度臭気が除去された被処理気体Gが、活性炭吸着塔53(活性炭により脱臭する脱臭設備)に供給されて低濃度臭気が脱臭された後、大気中に放出される。   According to this configuration, the high-concentration odor in the gas to be treated G is captured and removed by the sludge in the deodorization apparatus 1 regardless of the conventional high-concentration deodorization tower. And the to-be-processed gas G from which the high concentration odor and dust were removed is supplied to the medium concentration deodorization tower 52 (second deodorization device), and the medium concentration odor is deodorized. Subsequently, the to-be-processed gas G from which the medium concentration odor has been removed is supplied to the activated carbon adsorption tower 53 (deodorization equipment for deodorizing with activated carbon) to deodorize the low concentration odor, and then released into the atmosphere.

既存の返送汚泥ライン54は、汚泥を浄化処理工程の上流側に返送するため、気液混合した際に汚泥に捕捉された臭気成分を、浄化処理工程中に汚泥によって処理することができる。また、汚泥に含まれるアンモニアの濃度は低いため、臭気の主成分の一つであるアンモニアを捕捉し易い。   Since the existing return sludge line 54 returns the sludge to the upstream side of the purification treatment process, the odor component captured by the sludge when the gas and liquid are mixed can be treated with the sludge during the purification treatment process. Further, since the concentration of ammonia contained in the sludge is low, it is easy to capture ammonia which is one of the main components of odor.

また、図3に示す屎尿処理設備のように、脱臭装置1に供給する被処理気体Gとして、受入・前処理工程において発生する高濃度臭気を含む空気だけでなく、一次浄化処理工程において発生する中濃度臭気を含む空気を一緒に供給するように構成しても良い。   Further, as the manure processing facility shown in FIG. 3, the gas to be processed G supplied to the deodorizing apparatus 1 is generated not only in the air containing high-concentration odor generated in the acceptance / pretreatment process, but also in the primary purification process. You may comprise so that the air containing a medium concentration odor may be supplied together.

また、図4に示すように、屎尿処理設備が、堆肥を作るためのコンポスト化設備56を備える場合は、コンポスト化設備56から発生するコンポスト臭気及び粉塵を含む空気を被処理気体Gとして脱臭装置1に供給するように構成しても良い。尚、図4に示す屎尿処理設備では、受入・前処理工程において発生する高濃度臭気を含む空気が高濃度脱臭塔63によって一次処理される。また、一次浄化処理工程において発生した汚泥は、汚泥貯留槽や汚泥脱水機等を備える汚泥脱水設備55によって脱水処理された後、コンポスト化設備において堆肥とされる。   In addition, as shown in FIG. 4, when the manure processing facility includes a composting facility 56 for making compost, the deodorizing apparatus uses the air containing the compost odor and dust generated from the composting facility 56 as the processing gas G. 1 may be provided. In the manure processing facility shown in FIG. 4, the air containing the high concentration odor generated in the receiving / pretreatment step is primarily processed by the high concentration deodorization tower 63. Further, the sludge generated in the primary purification treatment process is dehydrated by a sludge dewatering equipment 55 including a sludge storage tank, a sludge dewatering machine, and the like, and then converted into compost in the composting equipment.

図5に示す屎尿処理設備では、受入・前処理工程において、受入槽40、貯留槽41、前貯槽57、前処理設備43、前脱水設備58等が使用される。また一次浄化処理工程において、脱窒素槽59、硝化槽60、二次脱窒素槽61、膜原水槽47(又は沈殿槽)、及び返送汚泥槽48等が使用される。   In the manure processing facility shown in FIG. 5, the receiving tank 40, the storage tank 41, the pre-storage tank 57, the pre-processing equipment 43, the pre-dehydration equipment 58, etc. are used in the receiving / pre-processing step. In the primary purification treatment step, a denitrification tank 59, a nitrification tank 60, a secondary denitrification tank 61, a membrane raw water tank 47 (or a precipitation tank), a return sludge tank 48, and the like are used.

図5の屎尿処理設備における一次浄化処理工程では活性汚泥処理及び脱窒処理が実施される。従って、当該屎尿処理設備は、返送汚泥ポンプによって返送汚泥槽48から脱窒素槽59に汚泥を返送する返送汚泥ライン54と、硝化液循環ポンプによって硝化槽60から脱窒素槽59に硝化液を返送する硝化液循環ライン62とを備えるものであり、上述の脱臭装置1が硝化液循環ライン62中に組み込まれている。尚、屎尿処理設備に既存の硝化液循環ポンプを使用することで、被処理気体Gと硝化液とを気液混合するための新たなポンプを設置する必要が生じない。   Activated sludge treatment and denitrification treatment are carried out in the primary purification treatment step in the manure treatment facility of FIG. Therefore, the sewage treatment equipment returns the nitrification liquid from the return sludge tank 48 to the denitrification tank 59 by the return sludge pump and the nitrification liquid from the nitrification tank 60 to the denitrification tank 59 by the nitrification liquid circulation pump. The deodorizing apparatus 1 described above is incorporated in the nitrifying liquid circulation line 62. In addition, it is not necessary to install a new pump for gas-liquid mixing of the gas G to be processed and the nitrification liquid by using the existing nitrification liquid circulation pump in the manure processing facility.

図5における脱臭装置1では、コンポスト化設備56から発生するコンポスト臭気及び粉塵を含む空気が被処理気体Gとして供給されると共に、硝化液循環ライン62によって返送される硝化液が臭気捕捉液Lとして供給される。従って、脱窒処理が行われる屎尿処理設備においては、硝化液を臭気捕捉液Lとして脱臭装置1に供給するように構成しても良い。尚、図5の屎尿処理設備では、受入・前処理工程における前脱水設備58から発生する汚泥がコンポスト化設備56により堆肥とされる。   In the deodorizing apparatus 1 in FIG. 5, air containing compost odor and dust generated from the composting equipment 56 is supplied as the gas to be treated G, and the nitrification liquid returned by the nitrification liquid circulation line 62 is used as the odor trapping liquid L. Supplied. Therefore, in a manure processing facility in which denitrification processing is performed, the nitrification liquid may be supplied to the deodorization apparatus 1 as the odor capturing liquid L. 5, the sludge generated from the pre-dehydration equipment 58 in the receiving / pre-treatment process is converted into compost by the composting equipment 56.

既存の硝化液循環ライン62は、硝化液を浄化処理工程の上流側に返送するため、気液混合した際に硝化液に捕捉された臭気成分を、浄化処理工程中に硝化液によって処理することができる。また、硝化液に含まれるアンモニアの濃度は低いため、臭気の主成分の一つであるアンモニアを捕捉し易い。   Since the existing nitrification liquid circulation line 62 returns the nitrification liquid to the upstream side of the purification treatment process, the odor component captured by the nitrification liquid when gas-liquid mixing is performed with the nitrification liquid during the purification treatment process. Can do. Further, since the concentration of ammonia contained in the nitrifying solution is low, it is easy to capture ammonia, which is one of the main components of odor.

以上のように、スクラバー方式の脱臭装置1を屎尿処理設備に組み込むことによって、被処理物を浄化する浄化処理工程の下流側から返送される汚泥又は硝化液に被処理気体Gが導入されて、前記汚泥又は硝化液と被処理気体Gとが気液混合された後、前記汚泥又は硝化液が前記浄化処理工程の上流側に戻されることになる。その結果、被処理気体Gと汚泥又は硝化液とが効率良く接触するため、被処理気体Gに含まれる、屎尿処理施設から排出される臭気(特に高濃度の臭気)や、粉塵が効率良く除去されて、被処理気体Gを清澄化することができる。   As described above, by incorporating the scrubber-type deodorizing apparatus 1 into the manure treatment facility, the gas to be treated G is introduced into the sludge or nitrification liquid returned from the downstream side of the purification treatment process for purifying the object to be treated, After the sludge or nitrifying liquid and the gas to be treated G are mixed in the gas-liquid state, the sludge or nitrifying liquid is returned to the upstream side of the purification process. As a result, since the gas to be treated G and sludge or nitrification liquid are in efficient contact with each other, the odor (particularly high-concentration odor) and dust contained in the gas to be treated G are efficiently removed. Thus, the gas G to be treated can be clarified.

また、脱臭装置1によって処理された後の被処理気体Gを、屎尿処理施設に設置される従来の脱臭塔(中濃度脱臭塔52、活性炭吸着塔53等)に供給して処理させれば、従来の脱臭塔の負荷を軽減することができる。従って、従来の脱臭塔の脱臭性能の低下を抑えることができると共に、脱臭に関する処理コスト(粉塵の除去が軽減される等のメンテナンスコストなど)を低減することも可能となり、また被処理気体Gをさらにより清澄化することができる。   Moreover, if the to-be-processed gas G processed by the deodorizing apparatus 1 is supplied and processed to the conventional deodorizing tower (medium concentration deodorizing tower 52, activated carbon adsorption tower 53 etc.) installed in the manure processing facility, The load on the conventional deodorizing tower can be reduced. Accordingly, it is possible to suppress a decrease in the deodorizing performance of the conventional deodorizing tower, and it is possible to reduce the processing cost related to the deodorization (maintenance cost such as reduction of dust removal), and the gas to be processed G can be reduced. It can be further clarified.

さらに、高濃度脱臭塔や中濃度脱臭塔といった高価な設備を、より安価なスクラバー方式の脱臭装置1に置き換えることが可能であり、設置コストを削減することもできる。   Furthermore, expensive equipment such as a high-concentration deodorization tower and an intermediate-concentration deodorization tower can be replaced with a cheaper scrubber-type deodorization apparatus 1, and the installation cost can be reduced.

また、屎尿処理施設等で使用される汚泥(活性汚泥など)や硝化液を臭気捕捉液として利用するため、臭気捕捉液を別途用意する必要がなく、効率的に脱臭処理を行うことができる。尚、汚泥の場合は、臭気が溶け込んだ汚泥が浄化処理工程の上流側から下流側に流下する過程において、臭気が分解され、その臭気が分解された汚泥を臭気捕捉液として利用するため、臭気捕捉液に臭気がより確実に捕捉される。また、硝化液の場合は、臭気が硝化液によって硝化されて硝化液に溶け込み易くなるため、硝化液によって臭気がより確実に捕捉される。   Moreover, since sludge (activated sludge etc.) and nitrification liquid used in a sewage treatment facility or the like are used as the odor trapping liquid, it is not necessary to separately prepare the odor trapping liquid, and the deodorization treatment can be performed efficiently. In the case of sludge, since the odor is decomposed in the process in which the sludge in which the odor is dissolved flows down from the upstream side to the downstream side of the purification treatment process, the sludge in which the odor is decomposed is used as the odor trapping liquid. Odor is more reliably captured in the capture liquid. Further, in the case of a nitrifying solution, the odor is nitrified by the nitrifying solution and easily dissolved in the nitrifying solution, so that the odor is more reliably captured by the nitrifying solution.

さらに、コンポスト化設備から排出される被処理気体、即ちコンポスト臭気の他に粉塵を多く含む被処理気体についても処理することが可能であるため、屎尿処理施設に対してコンポスト化設備を設置し易くなり、浄化処理及びコンポスト化処理の同時実施を促進することができる。   Furthermore, since it is possible to treat the gas to be treated discharged from the composting equipment, that is, the gas to be treated containing a lot of dust in addition to the compost odor, it is easy to install the composting equipment in the manure treatment facility. Thus, simultaneous implementation of the purification process and the composting process can be promoted.

〔その他の実施形態〕
1.上述の実施形態では、臭気除去部を2つ設ける構成を採用しているが、この構成に限定されるものではなく、必要に応じてさらにより多くの臭気除去部を設ける構成としても良いし、場合によっては一つだけの構成としても良い。
2.上述の実施形態では、気体供給口6を上壁2に設ける構成を採用しているが、この構成に限定されるものではなく、気体供給口6を左側壁3に設けるように構成しても良い。
3.上述の実施形態では、脱臭装置1に供給する被処理気体Gとして、高濃度臭気を含む空気、高濃度臭気及び中濃度臭気を含む空気、又はコンポスト臭気を含む空気を供給しているが、この構成に限定されるものではなく、被処理気体Gが、コンポスト臭気、浄化処理前の被処理物から生じる高濃度臭気、及び浄化処理中の被処理物から生じる中濃度臭気のうちの少なくとも一つを含むように構成して良い。
[Other Embodiments]
1. In the above-mentioned embodiment, although the structure which provides two odor removal parts is adopted, it is not limited to this structure, and it may be configured to provide even more odor removal parts as necessary. In some cases, only one configuration may be used.
2. In the above-described embodiment, the configuration in which the gas supply port 6 is provided in the upper wall 2 is adopted. However, the configuration is not limited to this configuration, and the gas supply port 6 may be provided in the left wall 3. good.
3. In the above-described embodiment, the gas to be treated G supplied to the deodorizing apparatus 1 is supplied with air containing high-concentration odor, air containing high-concentration odor and medium-concentration odor, or air containing compost odor. The gas G to be treated is not limited to the configuration, and at least one of the compost odor, the high concentration odor generated from the object to be processed before the purification process, and the medium concentration odor generated from the object to be processed during the purification process. You may comprise so that it may contain.

本発明に係る脱臭装置は、屎尿処理設備やコンポスト化設備から発生する臭気や粉塵を除去するだけでなく、工場から排出される排ガスの処理などにも適用することができる。   The deodorizing apparatus according to the present invention can be applied not only to removing odors and dusts generated from manure processing equipment and composting equipment, but also to treatment of exhaust gas discharged from a factory.

1 脱臭装置
2 上壁
3 左側壁
4 右側壁
5 底壁
6 気体供給口
7 気体排出口
8 液体供給口
9 液体排出口
10 液体排出機構
11〜15 第1〜第5仕切り壁
16 堰
21〜26 第1〜第6連通口
30 第1導入部
31 第1気液混合部
32 第2導入部
33 第2気液混合部
34 気液分離部
35 液体排出部
40 受入槽
41 貯留槽
42 予備貯留槽
43 前処理設備
44 深層反応槽
45 第1膜原水槽
46 第2膜原水槽
47 膜原水槽(又は沈殿槽)
48 返送汚泥槽
49 凝集混和槽
50 凝集膜原水槽(又は凝集沈殿槽)
51 高度処理設備
52 中濃度脱臭塔
53 活性炭吸着塔
54 返送汚泥ライン
55 汚泥脱水設備
56 コンポスト化設備
57 前貯槽
58 前脱水設備
59 脱窒素槽
60 硝化槽
61 二次脱窒素槽
62 硝化液循環ライン
63 高濃度脱臭塔
G 被処理気体
L 臭気捕捉液
S 接触面
DESCRIPTION OF SYMBOLS 1 Deodorizing apparatus 2 Upper wall 3 Left side wall 4 Right side wall 5 Bottom wall 6 Gas supply port 7 Gas discharge port 8 Liquid supply port 9 Liquid discharge port 10 Liquid discharge mechanism 11-15 First to fifth partition walls 16 Weirs 21 to 26 First to sixth communication ports 30 First introduction part 31 First gas-liquid mixing part 32 Second introduction part 33 Second gas-liquid mixing part 34 Gas-liquid separation part 35 Liquid discharge part 40 Receiving tank 41 Reserving tank 42 Preliminary reserving tank 43 Pretreatment equipment 44 Deep reaction tank 45 First membrane raw water tank 46 Second membrane raw water tank 47 Membrane raw water tank (or sedimentation tank)
48 Return sludge tank 49 Coagulation mixing tank 50 Coagulated membrane raw water tank (or coagulation sedimentation tank)
51 Advanced treatment equipment 52 Medium concentration deodorization tower 53 Activated carbon adsorption tower 54 Return sludge line 55 Sludge dewatering equipment 56 Composting equipment 57 Pre-storage tank 58 Pre-dehydration equipment 59 Denitrification tank 60 Nitrification tank 61 Secondary denitrification tank 62 Nitrification liquid circulation line 63 High concentration deodorization tower G Processed gas L Odor capture liquid S Contact surface

Claims (5)

被処理気体を臭気捕捉液中に導入する導入部と、前記被処理気体と前記臭気捕捉液との気液混合が行われて前記被処理気体中の臭気が除去される気液混合部とを備える脱臭装置において、
前記臭気捕捉液を前記導入部に供給するための液体供給口を、前記被処理気体と前記臭気捕捉液との接触面に対向する前記導入部の底壁に設けてあり、
前記導入部と前記気液混合部との間に仕切り壁が設けられており、前記仕切り壁の下に前記被処理気体及び前記臭気捕捉液が移動可能な連通口が設けられており、前記臭気捕捉液に導入された前記被処理気体が、前記連通口を通過して前記気液混合部に移動することを特徴とする脱臭装置。
An introduction part for introducing the gas to be treated into the odor capturing liquid, and a gas / liquid mixing part in which the gas to liquid mixing of the gas to be treated and the odor capturing liquid is performed to remove the odor in the gas to be treated. In the deodorizing device provided,
A liquid supply port for supplying the odor capture liquid to the introduction part is provided on the bottom wall of the introduction part facing the contact surface between the gas to be treated and the odor capture liquid;
A partition wall is provided between the introduction part and the gas-liquid mixing part, and a communication port through which the gas to be treated and the odor capturing liquid can move is provided under the partition wall, and the odor The deodorizing apparatus , wherein the gas to be treated introduced into the capture liquid passes through the communication port and moves to the gas-liquid mixing unit .
複数の前記導入部及び前記気液混合部を備え、前記被処理気体の前記臭気捕捉液への導入と、前記被処理気体と前記臭気捕捉液との気液混合が交互に行われるように構成されており、前記被処理気体が前記臭気捕捉液中に最初に導入される導入部の底壁にのみ前記液体供給口を設けてあることを特徴とする請求項1に記載の脱臭装置。   A plurality of the introduction part and the gas-liquid mixing part are provided, and the introduction of the gas to be treated into the odor trapping liquid and the gas-liquid mixing of the gas to be treated and the odor trapping liquid are alternately performed. The deodorizing apparatus according to claim 1, wherein the liquid supply port is provided only on a bottom wall of an introduction portion where the gas to be treated is first introduced into the odor trapping liquid. 流側に位置する仕切り壁の下端が、上流側に位置する仕切り壁の下端よりも高い位置に設定されており、下流側の連通口が上流側の連通口よりも大きくなるように設定されていることを特徴とする請求項2に記載の脱臭装置。 The lower end of the partition wall located on the lower stream side, is set at a position higher than the lower end of the partition wall located on the upstream side, is set as the communication port of the downstream side is larger than the communication port on the upstream side The deodorizing apparatus according to claim 2, wherein 前記被処理気体が、さらに粉塵を含むことを特徴とする請求項1〜3のいずれか1項に記載の脱臭装置。   The deodorizing apparatus according to any one of claims 1 to 3, wherein the gas to be treated further contains dust. 前記臭気捕捉液が、汚泥であることを特徴とする請求項1〜4のいずれか1項に記載の脱臭装置。   The deodorizing apparatus according to any one of claims 1 to 4, wherein the odor capturing liquid is sludge.
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