JPS6321312Y2 - - Google Patents

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Publication number
JPS6321312Y2
JPS6321312Y2 JP1986039876U JP3987686U JPS6321312Y2 JP S6321312 Y2 JPS6321312 Y2 JP S6321312Y2 JP 1986039876 U JP1986039876 U JP 1986039876U JP 3987686 U JP3987686 U JP 3987686U JP S6321312 Y2 JPS6321312 Y2 JP S6321312Y2
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JP
Japan
Prior art keywords
air
deodorizing
activated carbon
port
tower
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP1986039876U
Other languages
Japanese (ja)
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JPS61163033U (en
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Filing date
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Priority to JP1986039876U priority Critical patent/JPS6321312Y2/ja
Publication of JPS61163033U publication Critical patent/JPS61163033U/ja
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Expired legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)

Description

【考案の詳細な説明】 (産業上の利用分野) この考案はし尿処理或いは下水処理等で生ずる
悪臭空気の脱臭装置に係る。
[Detailed Description of the Invention] (Industrial Application Field) This invention relates to a deodorizing device for foul-smelling air generated in human waste treatment, sewage treatment, etc.

(従来の技術) この種の脱臭装置として活性炭粒を吸着材とす
ること、および該活性炭粒の再生装置を付設した
もの等はすでに周知である。
(Prior Art) This type of deodorizing device that uses activated carbon particles as an adsorbent and is equipped with a regenerating device for the activated carbon particles is already well known.

(考案が解決しようとする問題点) 上記従来のものはそれぞれの特性を有するも、
悪臭処理空気を先ず洗浄し、次いでその洗浄によ
る水分を排除し且つ除湿した後、常に層状に流動
する活性炭粒により悪臭の吸着を行ない、該吸臭
処理済みの活性炭を加熱により脱臭再生する手段
を一貫した連続装置としたものはなく、従つて従
来のものは連続作業としての効率は比較的低かつ
た。
(Problems to be solved by the invention) Although the above conventional methods have their own characteristics,
After first cleaning the malodor-treated air, then removing the moisture from the cleaning and dehumidifying it, the malodor is adsorbed by activated carbon particles that constantly flow in a layered manner, and the activated carbon that has been treated with odor absorption is heated to deodorize and regenerate it. There is no continuous equipment that can do this, and therefore, the efficiency of conventional equipment as a continuous operation was relatively low.

(問題点を解決するための手段) 本考案は前記洗浄、除湿、活性炭粒による吸臭
および活性炭粒の再生利用を一貫して連続的に円
滑に行なつて作業効率を向上させたもので、悪臭
処理空気の供給用フアンの吐気側に連通して該処
理空気の洗浄装置を設け、該洗浄装置の排気口に
連通する除湿装置の排気側をフアンを介して上部
に排気口を有する吸着装置の処理筒の下部送気口
に連通させ、該吸着装置の処理筒内にはその上部
排気口と下部連通口との間に粒状の活性炭を層状
に流動させる通気性の多孔板を交互に反対方向に
傾斜させて多段式に設け、その下部に連なる活性
炭粒の流下管を内部に加熱器を有し且つ脱臭用処
理空気を流通させた脱臭塔内に連通させると共に
該脱臭塔の下部排出口を還流管を経て前記多段式
流動板の上部に設けた活性炭粒の供給口に連通さ
せ、脱臭塔内上部と連通して脱臭処理済みの空気
を加熱除臭する脱臭分解炉を設けると共に該分解
炉の排気熱を利用した熱交換器を分解炉に連設
し、送風機からの送風を該熱交換器内を経て除湿
装置の機能再生部に吹込むようにして成る。
(Means for solving the problem) The present invention improves work efficiency by consistently and continuously performing the cleaning, dehumidification, odor absorption by activated carbon particles, and recycling of activated carbon particles. A cleaning device for the treated air is provided in communication with the discharge side of the fan for supplying the treated air, and the exhaust side of the dehumidifying device that communicates with the exhaust port of the cleaning device is connected to the adsorption device having an exhaust port at the top through the fan. The processing cylinder of the adsorption device is connected to the lower air supply port of the processing cylinder, and inside the processing cylinder of the adsorption device, between the upper exhaust port and the lower communication port, air-permeable perforated plates that flow granular activated carbon in a layered manner are arranged alternately in opposite directions. The activated carbon particles are installed in a multi-stage manner with an inclination to A deodorizing and decomposing furnace is provided which communicates with the activated carbon granule supply port provided at the upper part of the multi-stage fluidized plate through a reflux pipe and communicates with the upper part of the deodorizing tower to heat and deodorize the deodorized air. A heat exchanger that utilizes exhaust heat is connected to the decomposition furnace, and air from the blower is blown into the function regeneration section of the dehumidifier through the heat exchanger.

(実施例) 本考案の実施例とその作用を図面について説明
する。
(Example) An example of the present invention and its operation will be described with reference to the drawings.

し尿処理或いは下水処理場等からの悪臭空気は
フアン1によつて洗浄装置2に送込まれる。
Foul-smelling air from a human waste treatment plant or a sewage treatment plant is sent to a cleaning device 2 by a fan 1.

洗浄装置2は塔8内上部に散水管9を設け、そ
の下方に充填材層10を設けて散水管9から水を
散布し、充填材層10の充填材を濡らしつつ噴霧
状として塔8内下部から挿入されて上昇する悪臭
空気を洗浄するもので、この洗浄処理は水に限る
ことなく必要により酸、アルカリその他の薬液を
使用することができる。この洗浄処理により後で
行なう活性炭による吸着処理で吸着できないアン
モニア等のガスを除去し得る。
The cleaning device 2 is provided with a water spray pipe 9 in the upper part of the tower 8, and a filler layer 10 is provided below the water spray pipe 9, and water is sprayed from the water spray pipe 9 to wet the filler in the filler layer 10 and spray it into the tower 8. The purpose is to clean the foul-smelling air that is inserted from the bottom and rises.This cleaning process is not limited to water, but acids, alkalis, and other chemical solutions can be used as necessary. This cleaning process can remove gases such as ammonia that cannot be adsorbed by the activated carbon adsorption process that will be performed later.

このようにして洗浄処理を経て空気は多分に水
分を含有するため次いで除湿装置3に送込んで水
分を除くようにした。
After the cleaning process, the air contained a large amount of moisture, so it was then sent to the dehumidifier 3 to remove moisture.

除湿装置3は例えば内部に除湿剤を充填した回
転胴11を緩除に回転させ、その一面の一部から
他面に向つて処理空気を送込んで流通させること
により除湿剤により除湿するもので、回転胴11
の他部分においては一面から他面に向い再生用熱
風を送込んで流通させることにより除湿剤を乾燥
してその除湿能力を再生させるようにした乾式除
湿装置を使用する。洗浄次いで除湿された悪臭空
気は次いでフアン4により吸着装置5内に下部か
ら送込まれる。
The dehumidifier 3 dehumidifies with the dehumidifier by, for example, slowly rotating a rotary drum 11 filled with a dehumidifier inside, and blowing and circulating treated air from a part of one side toward the other side. , rotary cylinder 11
In other parts, a dry type dehumidifier is used which dries the dehumidifier and regenerates its dehumidifying ability by blowing and circulating hot air for regeneration from one side to the other. The cleaned and dehumidified foul-smelling air is then fed into the adsorption device 5 from below by the fan 4.

吸着装置5は処理塔12内上部に交互に反対方
向に傾斜させて多段式に設けた多孔板で形成した
流動板13の上部から粒状の活性炭を該流動板1
3に沿つて層状で順次下方に流動させるように構
成し、送込まれた悪臭空気はその多段層状の活性
炭と接触しつつ上昇する間に脱臭されて処理塔1
2の頂部の排気口14から排気される。
The adsorption device 5 supplies granular activated carbon to the fluidized plate 13 from the upper part of the fluidized plate 13, which is formed by a multi-stage perforated plate arranged at the upper part of the treatment tower 12 so as to be tilted alternately in opposite directions.
The foul-smelling air is deodorized while rising while coming into contact with the multilayered activated carbon, and passes through the treatment tower 1.
The air is exhausted from the exhaust port 14 at the top of 2.

処理塔12内で悪臭空気と接して悪臭気を吸着
した活性炭は順次塔12の下部から流下管15を
経て下面の脱臭塔6に送込まれる。
Activated carbon that has come into contact with malodorous air and adsorbed malodors in the treatment tower 12 is sequentially sent from the lower part of the tower 12 through the downflow pipe 15 to the deodorizing tower 6 on the lower surface.

脱臭塔6内には加熱蒸気管21より水蒸気を送
込んで加熱する加熱器16を備えて活性炭を加熱
すると共に処理塔6下部に開口した給気管17か
ら空気を圧入して活性炭から悪臭成分を脱着し、
その悪臭空気は脱臭塔6の上部より導出管22を
経て脱臭分解炉7に送られる。脱着により吸着機
能の再生した活性炭は脱臭塔6の底部から流下さ
せ、これを送風機18からの輸送用空気により還
流管19を経て処理塔12内の多段式傾斜流動板
13の上部供給口に還流させて供給し繰返して悪
臭の吸着処理に使用する。
The deodorizing tower 6 is equipped with a heater 16 that feeds steam through a heating steam pipe 21 to heat the activated carbon, and air is pressurized through an air supply pipe 17 opened at the bottom of the treatment tower 6 to remove malodorous components from the activated carbon. Attach and detach;
The foul-smelling air is sent from the upper part of the deodorizing tower 6 to the deodorizing decomposition furnace 7 through the outlet pipe 22. The activated carbon whose adsorption function has been regenerated by desorption is allowed to flow down from the bottom of the deodorizing tower 6, and is refluxed to the upper supply port of the multi-stage inclined fluidizing plate 13 in the treatment tower 12 via the reflux pipe 19 by the transport air from the blower 18. It is then repeatedly supplied and used for adsorption treatment of bad odors.

脱臭塔6から脱臭分解炉7に送られる空気の悪
臭成分は当初の吸臭処理前の濃度に対し100倍以
上に濃縮されて少量の空気に含まれるもので、こ
れを分解炉7内でオイルバーナー20で650℃以
上に加熱して高温で酸化分解させ、或いは触媒を
使用するときは250゜〜350℃の温度で熱分解させ
ることにより容易に悪臭を消失させ無臭として放
出するもので、この分解炉7における悪臭分解用
の熱を前記した除湿装置3の再生用熱風の加温用
として利用するため脱臭分解炉7の排気側にその
排気熱を熱源とする熱交換器23を連設し、除湿
装置3の再生用空気を送風機24により該熱交換
器23を通過させて加熱させるようにした。
The malodorous components of the air sent from the deodorizing tower 6 to the deodorizing decomposition furnace 7 are concentrated to more than 100 times the initial concentration before the odor absorption treatment, and are contained in a small amount of air. The odor is easily eliminated by oxidative decomposition at a high temperature of 650°C or higher at 20°C, or by thermal decomposition at a temperature of 250° to 350°C when a catalyst is used, and the odor is released as odorless. In order to use the heat for decomposing bad odors in the furnace 7 for heating the regenerating hot air of the dehumidifying device 3, a heat exchanger 23 using the exhaust heat as a heat source is connected to the exhaust side of the deodorizing decomposition furnace 7. The air for regeneration in the dehumidifier 3 was passed through the heat exchanger 23 by a blower 24 to be heated.

図中25はオイルバーナ20への燃料供給用ポ
ンプを示す。
In the figure, 25 indicates a pump for supplying fuel to the oil burner 20.

(考案の効果) 本考案によるときは洗浄と次いで除湿を行なつ
た悪臭空気を吸着装置に送込んで多段式に流動す
る活性炭層を向流させて接触させることにより吸
着処理を行なうため活性炭を固定させる式に比し
活性炭は交互に反対方向に傾斜させて多段式に設
けた多孔板で形成される流動面に沿い順次下方に
層状で移動するので活性炭と悪臭空気との接触効
率は向上し、又この際悪臭空気は予め除湿装置に
よる処理で水分は充分に除去されるため該処理空
気に含まれる水分の付着によつて脱臭作用効果が
低下し或いは該水分により粒状活性炭の粒子が崩
れる虞れはなく、吸着処理に使用した活性炭は順
次脱臭塔に移送してその活性を再生した後繰返し
吸着装置に供給して連続的に使用し、悪臭空気の
流れは常に活性の活発な活性炭に接触させるよう
にしたので、その吸着処理効果を著しく向上させ
ることができ、且つ活性炭を固定位置に置くもの
に比し、処理装置をコンパクト化し得るもので、
更に活性炭を再生した処理空気中の悪臭成分は当
初に比し少量の空気中に50〜100倍程度に濃縮さ
れているが、この脱臭処理済みの空気は脱臭分解
炉によつて高温で熱分解させて無臭として放出す
るため環境汚染の弊害を生ずることなく、更に脱
臭分解炉で処理空気の熱分解に使用した排気熱を
利用した熱交換器により加熱した空気を除湿装置
の機能再生部に吹込んで、除湿機能の再生効率を
高めたので、除湿装置による悪臭処理空気の除湿
作用を向上させ、従つて洗浄された後除湿された
悪臭処理空気に含まれる水分除去を更に的確と
し、活性炭が水分によつて崩壊し又活性炭の表面
に結露を生ずることを防止し得る効果を有する。
(Effects of the invention) According to the invention, the foul-smelling air that has been cleaned and then dehumidified is sent to an adsorption device and brought into contact with activated carbon layers flowing in multiple stages in countercurrent flow, thereby performing adsorption treatment. Compared to a fixed type, activated carbon moves downward in layers along the flow surface formed by multi-stage perforated plates that are tilted in opposite directions alternately, improving the contact efficiency between activated carbon and foul-smelling air. In addition, at this time, the foul-smelling air is treated with a dehumidifying device in advance to sufficiently remove moisture, so there is a risk that the deodorizing effect will decrease due to the adhesion of moisture contained in the treated air, or that the particles of granular activated carbon may collapse due to the moisture. The activated carbon used for adsorption treatment is sequentially transferred to a deodorizing tower to regenerate its activity and then repeatedly fed to the adsorption device for continuous use, so that the flow of foul-smelling air is always in contact with the active activated carbon. Since the activated carbon is placed in a fixed position, the adsorption treatment effect can be significantly improved, and the treatment equipment can be made more compact compared to the case where the activated carbon is placed in a fixed position.
Furthermore, the malodorous components in the treated air that has been regenerated from activated carbon are concentrated 50 to 100 times in a small amount of air compared to the initial amount, but this deodorized air is thermally decomposed at high temperatures in a deodorizing decomposition furnace. The air is heated by a heat exchanger that utilizes the exhaust heat used to thermally decompose the treated air in the deodorizing decomposition furnace, and is then blown into the functional regeneration section of the dehumidifier. By increasing the regeneration efficiency of the dehumidifying function, the dehumidifying effect of the dehumidifying device on the malodor-treated air is improved, and the water contained in the malodor-treated air that has been cleaned and dehumidified is more accurately removed. It has the effect of preventing dew condensation from being disintegrated on the surface of activated carbon.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本考案装置の実施例を示す系統線図であ
る。 1……処理悪臭空気の供給フアン、2……洗浄
装置、3……除湿装置、4……フアン、5……吸
着装置、6……脱臭塔、7……脱臭分解炉、12
……吸着装置の処理塔、13……多段式傾斜流動
板、16……加熱器、17……脱臭処理給気管、
23……熱交換器、24……送風機。
The drawing is a system diagram showing an embodiment of the device of the present invention. 1... Supply fan for treated malodorous air, 2... Cleaning device, 3... Dehumidifying device, 4... Fan, 5... Adsorption device, 6... Deodorizing tower, 7... Deodorizing decomposition furnace, 12
... Treatment tower of adsorption device, 13 ... Multi-stage inclined fluidized plate, 16 ... Heater, 17 ... Deodorizing treatment air supply pipe,
23...Heat exchanger, 24...Blower.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 悪臭処理空気の供給用フアンの吐気側に連通し
て該処理空気の洗浄装置を設け、該洗浄装置の排
気口に連通する除湿装置の排気側をフアンを介し
て上部に排気口を有する吸着装置の処理筒の下部
送気口に連通させ、該吸着装置の処理筒内にはそ
の上部排気口と下部連通口との間に粒状の活性炭
を層状に流動させる通気性の多孔板を交互に反対
方向に傾斜させて多段式に設け、その下部に連な
る活性炭粒の流下管を内部に加熱器を有し且つ脱
臭用処理空気を流通させた脱臭塔内に連通させる
と共に該脱臭塔の下部排出口を還流管を経て前記
多段式流動板の上部に設けた活性炭粒の供給口に
連通させ、脱臭塔内上部と連通して脱臭処理済み
の空気を加熱除臭する脱臭分解炉を設けると共に
該分解炉の排気熱を利用した熱交換器を分解炉に
連設し、送風機からの送風を該熱交換器内を経て
除湿装置の機能再生部に吹込むようにして成る空
気脱臭装置。
An adsorption device having a cleaning device for the treated air that communicates with the discharge side of a fan for supplying malodor-treated air, and an exhaust port at the top of the fan through which the exhaust side of a dehumidifier that communicates with the exhaust port of the cleaning device is provided. The processing cylinder of the adsorption device is connected to the lower air supply port of the processing cylinder, and in the processing cylinder of the adsorption device, between the upper exhaust port and the lower communication port, air permeable perforated plates that flow granular activated carbon in a layer are alternately arranged opposite to each other. A down-flow pipe for activated carbon particles connected to the bottom thereof is connected to a deodorizing tower which has a heater inside and circulates treated air for deodorizing, and a lower discharge port of the deodorizing tower. A deodorizing and decomposing furnace is provided which communicates with the upper part of the deodorizing tower and heats and deodorizes the deodorized air. An air deodorizing device comprising a heat exchanger that utilizes the exhaust heat of the furnace, which is connected to the decomposition furnace, and air from the blower is blown into the function regeneration section of the dehumidifier through the heat exchanger.
JP1986039876U 1986-03-20 1986-03-20 Expired JPS6321312Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1986039876U JPS6321312Y2 (en) 1986-03-20 1986-03-20

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1986039876U JPS6321312Y2 (en) 1986-03-20 1986-03-20

Publications (2)

Publication Number Publication Date
JPS61163033U JPS61163033U (en) 1986-10-09
JPS6321312Y2 true JPS6321312Y2 (en) 1988-06-13

Family

ID=30548236

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1986039876U Expired JPS6321312Y2 (en) 1986-03-20 1986-03-20

Country Status (1)

Country Link
JP (1) JPS6321312Y2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5440969B2 (en) * 2007-08-03 2014-03-12 千明 武内 Semi-wet adsorbent deodorization method
KR102405176B1 (en) * 2020-07-13 2022-06-07 한국에너지기술연구원 System for regeneration of activated carbon and method for regeneration of activated carbon
WO2024013973A1 (en) * 2022-07-15 2024-01-18 三菱電機株式会社 Carbon dioxide recovery device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5285072A (en) * 1976-01-08 1977-07-15 Kazuo Tashiro Deodorization column

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5285072A (en) * 1976-01-08 1977-07-15 Kazuo Tashiro Deodorization column

Also Published As

Publication number Publication date
JPS61163033U (en) 1986-10-09

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