JPH11342317A - Air cleaning device - Google Patents

Air cleaning device

Info

Publication number
JPH11342317A
JPH11342317A JP10166207A JP16620798A JPH11342317A JP H11342317 A JPH11342317 A JP H11342317A JP 10166207 A JP10166207 A JP 10166207A JP 16620798 A JP16620798 A JP 16620798A JP H11342317 A JPH11342317 A JP H11342317A
Authority
JP
Japan
Prior art keywords
harmful gas
reaction section
harmful gases
section
gas
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.)
Pending
Application number
JP10166207A
Other languages
Japanese (ja)
Inventor
Masanori Yoshinaga
正▲徳▼ 吉永
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP10166207A priority Critical patent/JPH11342317A/en
Publication of JPH11342317A publication Critical patent/JPH11342317A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the occurrence of the secondary pollution in an air cleaning device by providing this device with a reaction section where the harmful gases generated by decomposition and combustion of the org. matter mainly derived from living things are subjected to a non-polluting treatment under photoirradiation and an introducing section where the harmful gases are supplied under expansion in the reaction dection in the case of the cleaning of the harmful gases. SOLUTION: The air cleaning device 1 loaded horizontally between horizontal ducts where the harmful gases flow is provided with the introducing section 2 which supplies the harmful gases to the reaction section 5 at a lowered velocity while expanding the gases. Distribution plates 3,... are installed to the section and the respective one-side ends thereof are successively provided with flow regulating plates 4. The reaction section 5 provided with plural turbulence vent paths 8 laminated by shifting the phases of the amplitude of plural corrugated plates 7 of a triangular waveform by about 50% each to prevent the contact thereof with each other is included in such air purification device 1. The gas contact parts of these turbulence vent paths 8 are coated with titanium oxide surfaces 9 and plural photoirradiation lamps 10 isolated from the harmful gases by transparent protectors 11 are disposed at the proper points of the turbulence vent paths 8.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、下水処理場、し尿
処理場、生ゴミ集積場、堆肥化装置及び公衆便所や浄化
槽等から排出されるトリメチルアミン、メチルメルカプ
タン、硫化水素等や交通量の多い道路沿線や焼却場近辺
にある建物の空気調和設備に取り込まれたり、屋内駐車
場や地下自動車道などから排出される窒素酸化物、硫黄
酸化物、一酸化炭素及びダイオキシン等の有害物質など
を含む空気(以下有害ガスという)を酸化チタン光触媒
作用により乾式浄化する小型軽量で高性能な空気浄化装
置に関する。
The present invention relates to a sewage treatment plant, a human waste treatment plant, a garbage collection plant, a composting device, and trimethylamine, methyl mercaptan, hydrogen sulfide and the like discharged from public toilets and septic tanks, and a large amount of traffic. Contains harmful substances such as nitrogen oxides, sulfur oxides, carbon monoxide, and dioxin that are taken into the air conditioning equipment of buildings near roads and near incineration plants, and are emitted from indoor parking lots and underground motorways. The present invention relates to a small, lightweight, and high-performance air purification device for dry-purifying air (hereinafter referred to as harmful gas) by photocatalysis of titanium oxide.

【0002】[0002]

【従来の技術】従来の技術には、有害ガスを水やアルカ
リ溶液及び/又は酸溶液などの薬液に吸収及び反応させ
て除去する湿式法とオゾン又は化石燃料の燃焼高温ガス
に接触させるなどして分解処理する乾式法とがある。
2. Description of the Related Art Conventional techniques include a wet method in which harmful gas is absorbed and reacted with a chemical solution such as water or an alkaline solution and / or an acid solution, and contact with ozone or fossil fuel combustion hot gas. There is a dry method of decomposing.

【0003】また、該湿式法には、一般的に塔高が3〜
5m程度の水洗浄装置、酸洗浄装置等を順次組み合わせ
てなる処理システムや、アルカリ洗浄装置、酸洗浄装
置、活性炭吸着装置等を順次組み合わせてなる処理シス
テムなどがあり、有害ガスの処理効率を上げるために該
水洗浄装置、アルカリ洗浄装置及び酸洗浄装置には気−
液接触面積を大きくするラヒシリングのようなメディア
を、また活性炭吸着装置には活性炭を1.5 〜2m程度の
厚さで1段或は0.3 〜0.5 m程度の厚さで2〜3段に充
填する必要があり、総圧力損失を大きくすることから送
風装置の所要圧力は350〜500mmAq程度を要し、
所要馬力及び回転数を極めて大きなものにしていた。従
って、該送風装置の発する騒音・振動も大きな値とな
り、特に夜間における騒音規制値を守ることを難しく
し、そのために吸音材を内張りした壁厚が250〜30
0mmの鉄筋コンクリート製の防音室を要したり、更に、
敷地境界線沿に高い防音壁及び高木樹の植え込みも必要
となるばかりではなく、ガス流を介する共振音の発生を
防ぐための補強工事などをも必要としたり、或は全装置
を建家内に設置せざるを得なくなるなどの問題があっ
た。
[0003] The wet method generally has a tower height of 3 to 3 m.
There is a treatment system in which a water washing device and an acid washing device of about 5 m are combined in order, and a treatment system in which an alkali washing device, an acid washing device, an activated carbon adsorption device and the like are combined in order to increase the treatment efficiency of harmful gas. Therefore, the water cleaning device, the alkali cleaning device and the acid cleaning device are
It is necessary to fill a medium such as Lahishling to increase the liquid contact area, and to fill activated carbon in an activated carbon adsorption device in one stage with a thickness of about 1.5 to 2 m or in two or three stages with a thickness of about 0.3 to 0.5 m. In order to increase the total pressure loss, the required pressure of the blower needs about 350 to 500 mmAq,
The required horsepower and speed were extremely high. Therefore, the noise and vibration generated by the blower are also large, making it difficult to comply with the noise regulation value especially at night, and therefore, the wall thickness of the sound absorbing material is 250 to 30.
You need a soundproof room made of 0mm reinforced concrete,
Not only must high soundproof walls and high trees be planted along the site boundary, but also reinforcement work must be performed to prevent the generation of resonance noise through gas flow, or all equipment must be installed inside the building. There was a problem that it had to be installed.

【0004】また、該水洗浄装置、アルカリ洗浄装置及
び酸洗浄装置などにより吸収除去された有害成分は分解
されたものではなく、単に大気汚染物質を水質汚染物質
に転換しただけにすぎず、また吸収後液の排水処理には
その中に蓄積された反応生成物質が析出する前に越流排
出されるので中和処理も必要になるという問題があっ
た。
Further, the harmful components absorbed and removed by the water washing device, the alkali washing device and the acid washing device are not decomposed, but merely convert air pollutants into water pollutants. In the wastewater treatment of the liquid after absorption, there is a problem that a neutralization treatment is required since the reaction product accumulated in the liquid is overflowed before being precipitated.

【0005】更に、薬剤貯留装置、薬液稀釈や吸収後液
のPH調整装置、複数の吸収液循環ポンプや給排液ポン
プだけではなく、それらの装置と水洗浄装置又はアルカ
リ洗浄装置や酸洗浄装置及び活性炭吸着装置などの間を
結ぶ引廻ダクトと液配管及びそれらの支持・補強工事も
必要となるので、装置員数と建家及び機械基礎用土木工
事が増え、装置規模が大きくなり、広い敷地面積を要す
るなどのことから装置建設費が過大になるという問題も
あった。
[0005] Further, not only a drug storage device, a pH adjusting device for a solution diluted or absorbed after absorption, a plurality of absorption solution circulation pumps and supply / drainage pumps, but also those devices and a water washing device or an alkali washing device or an acid washing device In addition, the number of equipment, civil engineering work for buildings and machine foundations is increased, and the scale of the equipment is increased. There is also a problem that the equipment construction cost becomes excessive due to the required area.

【0006】従って、運転操作が繁雑になり人手が掛る
だけではなく、熟練者や専門技術者の常駐も必要とな
り、また吸収反応用の薬品ばかりではなく排液処理用の
中和剤や廃水処理用の薬品や活性炭などの消耗品代及び
電気消費料などが大きくなり、装置運転管理費が過大に
なるという問題もあった。
[0006] Accordingly, not only the operation becomes complicated and labor is required, but also a skilled person and a technician are required to be stationed, and not only the chemical for the absorption reaction but also the neutralizing agent for the drainage treatment and the wastewater treatment. There is also a problem that the cost of consumables such as chemicals for use and activated carbon, electric consumption, and the like increase, and the operation and management costs of the apparatus become excessive.

【0007】また、日常の入念な運転管理を怠ると直ち
に、大気汚染、水質汚染、騒音・振動などによる2次公
害の複合発生源施設になるという問題もあった。
[0007] Further, there is also a problem that, if negligible daily operation management is performed, the facility becomes a complex source facility of secondary pollution due to air pollution, water pollution, noise and vibration, and the like.

【0008】乾式法のオゾン処理システムは、弗素に次
ぐ極めて強い酸化分解力を持つオゾンを一般的には無声
放電方式のオゾン発生装置で発生させて有害ガスに接触
させて無害化処理するもので、原理が単純であるだけに
装置員数は少なく汚水も出ないという利点を持つが、オ
ゾンは保存が効ないこと、放電エネルギーのうちオゾン
生成には7.5 〜15%程度しか使われず、残りのエネル
ギーは熱に変りガス温度を上げてオゾン生成率を低下さ
せるために多量の冷却水が必要になり、また処理ガス中
の残存オゾンは極めて毒性の強い物質なので触媒作用が
付加された高価な特殊活性炭を消耗させながら無害化処
理するオゾンキラーが必要になるなどのことから運転管
理費が過大になるという問題があった。
A dry-type ozone treatment system generates ozone, which has an extremely strong oxidative decomposition power next to fluorine, generally by a silent discharge type ozone generator, and contacts the harmful gas to detoxify the ozone. Although the principle is simple, it has the advantage that the number of equipment is small and no sewage is generated. However, ozone is ineffective in storage, only about 7.5 to 15% of the discharge energy is used for ozone generation, and the remaining energy is used. A large amount of cooling water is required to reduce the ozone generation rate by raising the gas temperature by changing to heat, and expensive special activated carbon with a catalytic action is added because the residual ozone in the treated gas is an extremely toxic substance. There is a problem that an operation management cost is excessively large because an ozone killer for detoxifying the wastewater is required while the wastewater is consumed.

【0009】なお、高温燃焼処理システムは多量の重油
を燃焼させて有害ガスを高温で分解処理するもので、地
球を温暖化する二酸化炭素を多量に発生させ、また副生
する窒素及び硫黄の酸化物や煤煙を除去する脱硫・脱硝
装置や集塵装置などが必要になり装置建設費及び運転管
理費が過大になるなどの問題があった。
The high-temperature combustion processing system burns a large amount of heavy oil to decompose harmful gas at a high temperature, generates a large amount of carbon dioxide that warms the earth, and oxidizes by-product nitrogen and sulfur. A desulfurization / denitration device and a dust collection device for removing substances and soot are required, and there is a problem that the device construction cost and operation management cost become excessive.

【0010】[0010]

【発明が解決しようとする課題】本発明が解決しようと
する課題は、有害ガスを無害化処理する空気浄化装置が
2次公害源になり易く、また装置建設費及び運転管理費
が過大になる点である。
SUMMARY OF THE INVENTION The problem to be solved by the present invention is that an air purification device for detoxifying harmful gas tends to be a secondary pollution source, and the construction cost and operation management cost become excessive. Is a point.

【0011】[0011]

【課題を解決するための手段】上記課題を解決するため
の本発明は、主に生物に由来する有機物の分解や燃焼な
どに伴ない発生した有害ガスを浄化する空気浄化装置に
おいて、該有害ガスを光照射しながら無害化処理する反
応部と該反応部に有害ガスを膨張させながら供給する導
入部とを具備し、該反応部が導入部から供給された有害
ガスに乱流を与える複数の乱流通気路を備え、該乱流通
気路が複数の波状板を互に接触しないように積層してな
り、該乱流通気路の接ガス部が酸化チタンで被覆され、
該乱流通気路内に複数の光照射ランプが装設されている
ことを特徴とする空気浄化装置である。
According to the present invention, there is provided an air purifying apparatus for purifying harmful gas mainly generated by decomposition or combustion of organic matter derived from living organisms. A reaction section for detoxifying the harmful gas while irradiating light, and an introduction section for supplying a harmful gas to the reaction section while expanding the reaction section, wherein the reaction section provides a turbulent flow to the harmful gas supplied from the introduction section. With a turbulent air path, the turbulent air path is laminated so that a plurality of corrugated plates do not contact each other, and the gas contact portion of the turbulent air path is coated with titanium oxide,
An air purification device, wherein a plurality of light irradiation lamps are provided in the turbulent air passage.

【0012】また、該光照射ランプが透明な保護体によ
り有害ガスから隔離され随時装脱着可能に装設されてい
ることを特徴とする空気浄化装置である。
Further, the air purifying apparatus is characterized in that the light irradiation lamp is separated from harmful gas by a transparent protective body and is detachably mounted at any time.

【0013】[0013]

【発明の実施の形態】上記のように構成された空気浄化
装置は、主に生物に由来する有機物質の醗酵、腐敗及び
燃焼などに伴ない生ずる気体、例えば生ゴミの集積場や
焼却場、堆肥化装置及び屋内駐車場や地下自動車道など
で発生するトリメチルアミン、メチルメルカプタン、窒
素酸化物、一酸化炭素、ダイオキシンなどを含む有害ガ
スを、反応部を構成し接ガス部が酸化チタンで被覆され
且つその内部に光照射ランプが装設された複数の乱流通
気路に分配しながら流通させるとともに光照射し、受光
した酸化チタン面に瞬時に発現することが知られている
酸化チタン光触媒作用によって直接的に分解し乾式浄化
処理するので、装置の構造を単純にでき、また操作が簡
単になり送風装置と光照射ランプのスイッチを入れるだ
けで容易に起動できるだけでなく始動直後に最大負荷運
転に入れる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The air purifying apparatus constructed as described above is mainly used for accumulating or incinerating garbage, such as gas produced by fermentation, spoilage and combustion of organic substances derived from living organisms. A harmful gas containing trimethylamine, methyl mercaptan, nitrogen oxide, carbon monoxide, dioxin, etc. generated in composting equipment and indoor parking lots and underground roads, etc. constitutes a reaction part and the gas contact part is coated with titanium oxide The titanium oxide photocatalyst, which is known to be instantaneously expressed on the surface of the titanium oxide that has been irradiated with light while being distributed while being distributed to a plurality of turbulent air passages provided with a light irradiation lamp therein, is known. Since it is directly decomposed and dry-cleaned, the structure of the device can be simplified, and the operation is simple. Add to maximum load operation immediately after the start, not only that.

【0014】また、反応部を構成する複数の乱流通気路
が、三角波状、台形波状、サインカーブを示すうねり波
状、平板状及びそれらを適宜に組み合わせた形状などを
有する複数の波状板を互に接触しないように積層してな
る空の気道状空間なので、酸化チタン光触媒作用が発現
する酸化チタン面が大きくできるだけでなく、有害ガス
流に乱流を与えて酸化チタン面に浄化されたガスが纏わ
りつくのを防ぐ気−固境面刷新作用を発現させることに
より浄化能力が高められ、浄化所要時間が短縮されて装
置を小型化できる。
Further, the plurality of turbulent air paths constituting the reaction section are formed by alternately connecting a plurality of corrugated plates having a triangular wave shape, a trapezoidal wave shape, a wave shape showing a sine curve, a flat plate shape, and a shape obtained by appropriately combining them. Because it is an empty airway-like space that is laminated so that it does not contact the surface, not only can the titanium oxide surface where the titanium oxide photocatalysis develops be large, but also the turbulent flow to the harmful gas flow and the purified gas on the titanium oxide surface By exhibiting a gas-solid surface renewal effect of preventing the entanglement, the purification ability is enhanced, the time required for purification is shortened, and the apparatus can be downsized.

【0015】そして、反応部を構成する複数の乱流通気
路が複数の波状板を互に接触しないように積層してなり
且つ接ガス部が酸化チタンで被覆され、内部に光照射ラ
ンプが装設されただけの圧力損失の小さな空の気道状空
間であり、有害ガスを受光した酸化チタン面に瞬時に発
現する酸化チタン光触媒作用により直接的に分解し乾式
浄化するなどのことから、ラヒシリングのようなガス流
及び光を遮り圧力損失を高める充填材及び酸やアルカリ
などの吸収薬液は一切使用しないので、送風装置の送風
圧力、出力及び回転数を小さくでき、また吸収塔は素よ
り薬品の貯留、濃度調整、給排、循環、中和及び廃水処
理などの液体系の付帯装置は全く無用になり、電力、薬
品及び水などの用役費用が削減でき、騒音・振動値が小
さく廃水も出ない無公害システムにすることができ、装
置員数も少なくできるなどのことから装置の所要敷地面
積、建設費及び運転管理費などを小さくでき、省力化、
省エネルギー化、省資源化、及び無公害化が計られる。
A plurality of turbulent air passages constituting the reaction section are laminated such that a plurality of corrugated plates are not in contact with each other, and the gas contacting section is covered with titanium oxide, and a light irradiation lamp is mounted inside. It is an empty airway-like space with a small pressure loss just installed, and it is directly decomposed and dry-purified by the titanium oxide photocatalytic action that instantaneously appears on the titanium oxide surface that received the harmful gas. The use of such fillers that block gas flow and light and increase pressure loss and absorbent chemicals such as acids and alkalis are not used at all, so that the blowing pressure, output and rotation speed of the blower can be reduced, and the absorption tower is more effective than chemicals for absorbing chemicals. Liquid-related auxiliary equipment such as storage, concentration adjustment, supply / discharge, circulation, neutralization, and wastewater treatment are completely unnecessary, and utility costs such as electricity, chemicals and water can be reduced, and noise and vibration values are small and wastewater can be used. Does not appear It can be pollution system, the required land area of the device since such devices Number can also reduce, can be reduced and construction costs and operation and management costs, labor saving,
Energy saving, resource saving, and pollution-free are to be achieved.

【0016】さらに、反応部を構成する複数の乱流通気
路が厚さの薄い複数の波状板を互に接触しないように積
層してなる多層構造体なので、その両端に位置する2枚
の波状板以外は表裏両面が有効な共通仕切板となり、乱
流通気路の総容積に占める酸化チタンの被覆総面積の比
率が高められ、また波状板の所要数が常に有害ガスの処
理に要する乱流通気路の総数に対して1を加えた枚数で
賄えるので乱流通気路の所要数が増る程に波状板の所要
数は逓減するなどのことから、装置の軽量化と小型大容
量化とが計られる。
Further, since the plurality of turbulent air paths constituting the reaction section are formed by laminating a plurality of thin corrugated plates so as not to contact each other, two corrugated sheets located at both ends thereof are provided. Except for the plate, both front and back sides are effective common partition plates, the ratio of the total area of titanium oxide coating to the total volume of the turbulent air passage is increased, and the required number of corrugated plates is always the turbulent flow required for harmful gas treatment Since the number of airways can be covered by 1 plus the required number of turbulent airways, the required number of corrugated plates gradually decreases as the required number of turbulent airways increases. Is measured.

【0017】また、反応部を構成する複数の乱流通気路
の形状が、気−固境面刷新作用を律するので三角波状、
台形波状、サインカーブを示すうねり波状、平板状など
及びそれらを適宜に組み合わせた形状の波状板の中から
最適なものが選べること、更に同じ波形、波長、振幅の
波状板を互に接触しないようにするとともに隣り合うも
の同志の振幅位相を同じくし又は規則的にずらし且つ振
幅軸が平行になるように積層したり、波形は同じでも波
長及び/又は振幅の異なる波状板を適宜に組み合わせ且
つ振幅軸が平行になるように積層したり、波形、波長、
振幅ともに異なる波状板を適宜に組み合わせ且つ振幅軸
が平行になるように積層したり、或はそれらの振幅軸が
交差するように積層したりなどすることにより千差万別
のものができるので、その中から有害ガスの処理量、組
成及び濃度などに応じ最適なものを選定し得ることか
ら、適用分野を広げることができる。
Further, since the shape of the plurality of turbulent air passages constituting the reaction section governs the air-solid surface renewal operation, a triangular wave,
Trapezoidal wave, undulating wave showing sine curve, flat plate etc. and appropriate combination of them can be selected from the best, and furthermore, do not touch the corrugated plates with the same waveform, wavelength and amplitude In addition, adjacent ones are laminated such that the amplitude phases of adjacent ones are the same or regularly shifted and the amplitude axes are parallel, or wave-shaped plates having the same waveform but different wavelengths and / or amplitudes are appropriately combined and amplitudes are adjusted. Laminating so that the axes are parallel, waveform, wavelength,
By properly combining corrugated plates with different amplitudes and laminating them so that their amplitude axes are parallel, or by laminating them so that their amplitude axes intersect, a variety of different things can be made. From these, the most suitable one can be selected according to the processing amount, composition, concentration, etc. of the harmful gas, so that the field of application can be expanded.

【0018】さらに、波状板の表面に茸状、多角錐状、
縦縞状、横縞状など及びそれらを適宜に組み合わせた小
凸起を設けることによりガス流速に応じた渦流を発生さ
せて乱流様態を変えることができるので、負荷変動に対
し自律的に即応させることができる。
Further, mushroom-like, polygonal pyramid-like,
By providing vertical stripes, horizontal stripes, etc. and small projections appropriately combining them, it is possible to generate a vortex according to the gas flow velocity and change the turbulence mode, so that it can respond autonomously to load fluctuations Can be.

【0019】また、接ガス部が酸化チタンで被覆された
複数の乱流通気路と光照射ランプとを備えた反応部は、
酸化チタン面が受光し発現する酸化チタン光触媒作用に
より活性酸素を発するので、ウィルス、細菌などを不活
性化、殺菌することができ、またオゾンガスのような有
害物質は副生されないので居住空間の循環空気の浄化に
も使うことができる。
Further, the reaction section having a plurality of turbulent air passages whose gas contact portions are coated with titanium oxide and a light irradiation lamp,
Active oxygen is emitted by the titanium oxide photocatalyst that is received and expressed by the titanium oxide surface, so that viruses and bacteria can be inactivated and sterilized. Also, harmful substances such as ozone gas are not produced as by-products, so circulation in living spaces It can also be used for air purification.

【0020】そして、光照射ランプが透明保護体により
有害ガス流から隔離されているのでケースの外から随時
にランプ交換でき、また寿命が6,000 〜9,000 時間なの
で殆んどメンテナンスフリーの長期連続運転をすること
ができる。
Since the light irradiation lamp is isolated from the harmful gas flow by the transparent protective body, the lamp can be replaced at any time from the outside of the case, and since the life is 6,000 to 9,000 hours, almost maintenance-free long-term continuous operation is possible. can do.

【0021】さらに、光照射ランプに照度調整器及び集
中監視盤に端末を接続したランプ切表示器を設けること
により無人運転をすることができる。
Further, by providing a light irradiation lamp with an illuminance adjuster and a lamp-off indicator with a terminal connected to a centralized monitoring panel, unmanned operation can be performed.

【0022】[0022]

【実施例】本発明の第1実施例を断面図を示した図1に
基づいて説明する。1は有害ガスの流れる水平ダクト間
に横向に装設した空気浄化装置である。2は該有害ガス
を膨張させながら流速を下げて反応部5に供給する導入
部であり、分配板3が付設されている。4は整流板であ
り、その一端部と分配板3の一端部とが連接している。
反応部5には三角波状の複数の波状板7を互に接触しな
いようにし、且つその振幅の位相を50%づつずらし積
層してなる複数の乱流通気路8が設けられている。6は
ケース、9は乱流通気路8の接ガス部を被覆した酸化チ
タン面である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described with reference to FIG. Reference numeral 1 denotes an air purification device installed horizontally between horizontal ducts through which harmful gas flows. Reference numeral 2 denotes an introduction section which supplies the reaction gas to the reaction section 5 at a reduced flow rate while expanding the harmful gas, and is provided with a distribution plate 3. Reference numeral 4 denotes a current plate, one end of which is connected to one end of the distribution plate 3.
The reaction section 5 is provided with a plurality of turbulent air passages 8 formed by laminating a plurality of triangular wavy plates 7 so as not to contact each other and shifting the amplitude phases thereof by 50%. Reference numeral 6 denotes a case, and 9 denotes a titanium oxide surface covering the gas contact portion of the turbulent air passage 8.

【0023】10は光照射ランプであり、透明保護体1
1により有害ガスから隔離され、運転中にもケースの外
から随時ランプ交換できるように装設され、ケースの側
面には図示しないランプ点検口が設けられている。導出
部12には抵抗板13が設けられ、無害化処理した浄化
ガスを収縮させながら排出する。なお、抵抗板13は乱
流通気路8内を流れるガス量及び速度を調節し渦流の発
生状態を変えて処理性能を高水準に安定化させる。ま
た、波状板7の一端部は整流板4の他端部に連接し、他
端部は抵抗板13の一端部に連接している。
Reference numeral 10 denotes a light irradiation lamp, and the transparent protective body 1
1 is provided so that the lamp can be replaced at any time from outside the case even during operation, and a lamp inspection port (not shown) is provided on the side of the case. A resistance plate 13 is provided in the lead-out section 12, and discharges the detoxified purified gas while shrinking. The resistance plate 13 regulates the amount and speed of gas flowing in the turbulent air passage 8 to change the state of vortex generation, thereby stabilizing the processing performance to a high level. One end of the corrugated plate 7 is connected to the other end of the rectifying plate 4, and the other end is connected to one end of the resistance plate 13.

【0024】また、有害ガス中にミストや水蒸気及び付
着性物質などが含まれる場合には、反応部を傾設して波
状板7の凹部をドレンの導出溝に見倣してその下端部を
結ぶ集水溝とドレンポットとを設ける。なお、Aは有害
ガスの流れる方向を示す矢印、Bは無害化処理された浄
化ガスの流れる方向を示す矢向である。
When the harmful gas contains mist, water vapor, or an adhering substance, the reaction section is inclined to imitate the concave portion of the corrugated plate 7 as a drain outlet groove, and the lower end thereof is formed. A connecting water collecting groove and a drain pot are provided. Note that A is an arrow indicating the direction in which the harmful gas flows, and B is an arrow direction indicating the direction in which the detoxified purified gas flows.

【0025】本発明の第2実施例を断面図を示した図2
に基づいて説明する。14は小型の空気浄化装置であ
り、15は分配板16が設けられた導入部、17は2本
の乱流通気路20を備えた反応部、19は台形波状の波
状板である。乱流通気路20は2枚の波状板19に接触
しないようにして中央分離帯状に設けた照光群体22で
分割し形成されている。21は乱流通気路20の接ガス
部の酸化チタン面である。23は照光群帯22の図示し
ない案内溝沿に装設された光照射ランプである。24は
透明保護体であり、有害ガス流から光照射ランプ23を
隔離している。なお、光照射ランプ23はケースの図示
しない側面に設けたランプ点検口から運転を中断するこ
となく随時に取り替ることができる。26は仕切板27
が設けられた導出部である。
FIG. 2 is a sectional view showing a second embodiment of the present invention.
It will be described based on. 14 is a small-sized air purification device, 15 is an introduction portion provided with a distribution plate 16, 17 is a reaction portion provided with two turbulent air passages 20, and 19 is a trapezoidal wavy plate. The turbulent air passage 20 is divided by an illuminating group 22 provided in the form of a central separation band so as not to contact the two corrugated plates 19. Reference numeral 21 denotes a titanium oxide surface of a gas contact portion of the turbulent air passage 20. Reference numeral 23 denotes a light irradiation lamp provided along a guide groove (not shown) of the illumination group 22. Reference numeral 24 denotes a transparent protective body, which isolates the light irradiation lamp 23 from the harmful gas flow. The light irradiation lamp 23 can be replaced at any time from a lamp inspection port provided on a side surface (not shown) of the case without interrupting the operation. 26 is a partition plate 27
Is a derivation unit provided with.

【0026】本発明の第3実施例を断面図を示した図3
に基づいて説明する。27は竪型の空気浄化装置であ
り、28は分配板29が設けられた導込部、30は複数
の乱流通気路33を備えた反応部、32は三角波状の複
数の波状板である。乱流通気路33は複数の波状板32
を互に接触しないように且つ波長位相を順次規則的にず
らして積層し形成されている。34は乱流通気路33の
接ガス部の酸化チタン面である。35は乱流通気路33
の拡張空間中央部に装設された光照射ランプであり、透
明保護体36により有害ガス流から隔離され、ケースの
図示しない側面に設けたランプ点検口から運転中にも装
脱着可能に装設されている。37は抵抗板38が設けら
れた導出部であり、浄化ガス中の花粉や媒塵などをダス
トチャンバ39に導びく。40は分気口41と排出口4
2とを繋ぐ導気路、43は排塵蓋44を設けた除塵口で
ある。波状板33は一端部が分配板30と他端部が抵抗
板39とに連接している。また、波状板32と分配板2
9及び/又は抵抗板38との間に整流板を設けても、ダ
ストチャンバ39に水を張ったり、水噴霧したり或はエ
アフイルタを設けてもよい。なお、Cは除塵浄化ガスの
流れる方向を示す矢印である。
FIG. 3 is a sectional view showing a third embodiment of the present invention.
It will be described based on. 27 is a vertical type air purification device, 28 is a guiding portion provided with a distribution plate 29, 30 is a reaction portion provided with a plurality of turbulent air passages 33, and 32 is a plurality of triangular wavy plates. . The turbulent air passage 33 includes a plurality of corrugated plates 32.
Are laminated so that they do not contact each other and the wavelength phases are sequentially shifted regularly. Reference numeral 34 denotes a titanium oxide surface of a gas contact portion of the turbulent air passage 33. 35 is a random circulation airway 33
A light irradiating lamp installed in the center of the expansion space. The light irradiating lamp is isolated from the harmful gas flow by a transparent protective body 36, and is installed and detached during operation from a lamp inspection port provided on a side surface (not shown) of the case. Have been. Reference numeral 37 denotes a lead-out portion provided with a resistance plate 38, which guides pollen, dust and the like in the purified gas to a dust chamber 39. 40 is a vent 41 and an outlet 4
Reference numeral 43 denotes a dust removal port provided with a dust cover 44. One end of the corrugated plate 33 is connected to the distribution plate 30 and the other end is connected to the resistance plate 39. Further, the corrugated plate 32 and the distribution plate 2
A flow straightening plate may be provided between the dust chamber 9 and / or the resistance plate 38, or the dust chamber 39 may be filled with water, sprayed with water, or provided with an air filter. C is an arrow indicating the direction in which the dust-removing purification gas flows.

【0027】本発明の第4実施例を断面図を示した図4
に基づいて説明する。45は縦置した大容量省スペース
型の空気浄化装置であり、第1反応部48Aと第2反応
部48Bとが設けられている。46は往送分配板47を
備えた導入部、50は複数の平板51でなる複数の空間
をそれぞれ三角波状の波状板52A,52Bで互が接触
しないように一定間隔を置いて仕切り形成した複数の乱
流通気路であり、53は接ガス部の酸化チタン面であ
る。55は光照射ランプ54を有害ガス流から隔離する
透明保護体であり、ケースの図示しない側面に設けたラ
ンプ点検口から運転中でも随時装脱着可能に装設されて
いる。56は第1反応部48Aから導出されたガスを第
2反応部48Bに供給する折返部であり、転送抵抗板5
7と復送分配板58とが設けられている。59は浄化ガ
スを排出する導出部であり、排送抵抗板60が設けられ
ている。
FIG. 4 is a sectional view showing a fourth embodiment of the present invention.
It will be described based on. A large-capacity, space-saving air purification device 45 is provided vertically, and is provided with a first reaction section 48A and a second reaction section 48B. Reference numeral 46 denotes an introduction portion provided with a forward distribution plate 47, and reference numeral 50 denotes a plurality of spaces formed by partitioning a plurality of spaces formed by a plurality of flat plates 51 at predetermined intervals so as not to be in contact with each other by triangular wavy plates 52A and 52B. And 53 is a titanium oxide surface of a gas contact portion. Reference numeral 55 denotes a transparent protector for isolating the light irradiation lamp 54 from the harmful gas flow, and is provided so as to be detachable at any time during operation from a lamp inspection port provided on a side surface (not shown) of the case. Reference numeral 56 denotes a turn-back section for supplying gas derived from the first reaction section 48A to the second reaction section 48B.
7 and a return distribution plate 58 are provided. Reference numeral 59 denotes a lead-out unit that discharges the purified gas, and is provided with a discharge resistance plate 60.

【0028】また、波状板52Aは、一端部が往送分配
板47の一端部に、他端部が転送抵抗板57の一端部に
連接している。波状板52Bは一端部が復送分配板58
の一端部に、他端部が排送抵抗板60の一端部に連接し
ている。また、整流板を波状板52Aと往送分配板47
及び/又は転送抵抗板57との間に設けても、波状板5
2Bと復送分配板58及び/又は排送抵抗板60との間
に設けてもよい。なお、Dは1次浄化ガスの流れる方向
を示す矢印である。
The corrugated plate 52A has one end connected to one end of the forward distribution plate 47 and the other end connected to one end of the transfer resistance plate 57. One end of the corrugated plate 52B has a return distribution plate 58.
The other end is connected to one end of the discharge resistance plate 60. In addition, the rectifying plate is composed of the corrugated plate 52A and the forward distribution plate 47.
And / or between the transfer resistor plate 57 and the corrugated plate 5.
2B and the return distribution plate 58 and / or the discharge resistance plate 60 may be provided. D is an arrow indicating the direction in which the primary purification gas flows.

【0029】本発明の第1実施例の空気浄化装置1は主
に、生ごみ集積場、堆肥化装置、し尿処理装置の臭気分
岐ダクトなどに個々に取り付ける簡易的用途に適し、第
2実施例の空気浄化装置14は主に、アレルギーや喘息
等の原因になるホルムアルデヒドのような化学物質、だ
にやかびや耐性菌等の生物やそれらに由来する物質を含
む室内空気を浄化する病室や地下室などの循環処理用や
厨房、便器及び便所の脱臭用などに適し、第3実施例の
空気浄化装置は主に、自動車排気ガスやダイオキシンを
含む燃焼ガスなどに汚染された外気を取り込む学校、病
院、オフィスビル等の空気調和用に適し、第4実施例の
空気浄化装置は、地下駐車場、地下自動車道等の集中排
気処理、生ごみ集積場、し尿処理場、下水処理場、堆肥
化装置等の集中脱臭処理などに適している。
The air purifying apparatus 1 according to the first embodiment of the present invention is mainly suitable for a simple application individually attached to a garbage collection point, a composting apparatus, an odor branch duct of a human waste treatment apparatus, and the like. The air purifying device 14 is mainly used for purifying indoor air containing chemical substances such as formaldehyde that causes allergies and asthma, living organisms such as mushrooms and resistant bacteria, and substances derived therefrom. The air purifying apparatus of the third embodiment is suitable for circulation treatment of kitchens, toilets and toilets, etc., and is mainly used for schools and hospitals that take in outside air contaminated with automobile exhaust gas or combustion gas containing dioxin. The air purifying apparatus of the fourth embodiment is suitable for air conditioning of office buildings, etc., and is used for centralized exhaust treatment of underground parking lots, underground motorways, etc., garbage collection facilities, human waste treatment facilities, sewage treatment facilities, composting equipment Decentralization It is suitable for such treatment.

【0030】本発明は上述の図1〜図4に示した実施例
に限定されるものではなく、波状板7、19、32、5
2A、52Bの波形は三角波状や台形波状の代りにサイ
ンカーブを描くうねり波状及びそれらを適宜に組み合わ
せたものでも、更に該波状板の表面に茸状、多角錐状、
縦縞状、横縞状及びそれらを適宜に組み合わせた小凸起
などを設けてもよく、積層されて乱流通気路7、19、
32、52A、53Aを形成する波状板は隣り合うもの
同志の波形、波長、及び振幅が全て同一のものの代りに
波形が相異するものであっても、或は同じ波形であって
も波長及び/又は振幅が相異するものであってもよく、
また積層した波状板を複数の貫通棒とスペイサとで整流
スリット状に支持してもよい。
The present invention is not limited to the embodiment shown in FIGS. 1 to 4 described above.
The waveforms of 2A and 52B are not only triangular waveforms or trapezoidal waveforms but also undulating waveforms that draw a sine curve and those appropriately combined, and furthermore, mushroom shapes, polygonal pyramids,
Vertical stripes, horizontal stripes, and small protrusions or the like obtained by appropriately combining the stripes may be provided.
The corrugated plates forming 32, 52A, and 53A have different waveforms, wavelengths, and amplitudes of adjacent ones instead of all having the same waveform, or have the same wavelength, even if they have the same waveform. And / or may have different amplitudes,
Further, the laminated corrugated plate may be supported in a rectifying slit shape by a plurality of through bars and a spacer.

【0031】また、光照射ランプ10、23、35、5
4に照度調整器を付設し、更に集中監視盤に端末を接続
したランプ切表示器などを設けてもよく、有害ガス中の
ダスト濃度が高い場合や含水分が多い場合には前処理用
に除塵装置や除湿装置及び乱流通気路の洗浄装置などを
設けてもよく、従来法の装置の増強に適宜組み込んでも
よくその他本発明の要旨を逸脱しない範囲内で種々変更
を加え得ることは勿論である。
The light irradiation lamps 10, 23, 35, 5
An illuminance adjuster may be attached to 4, and a centralized monitoring panel may be equipped with a lamp-off indicator connected to a terminal. If the dust concentration in the harmful gas is high or the moisture content is high, use it for pretreatment. A dust removing device, a dehumidifying device, a cleaning device for a turbulent air passage, and the like may be provided, and may be appropriately incorporated into an enhancement of a conventional method, and various other changes may be made without departing from the scope of the present invention. It is.

【0032】次に、上記のように構成された本発明の空
気浄化装置により実施した臭気ガス浄化処理の実験結果
を表1の「臭気ガス浄化試験」に示す。
Next, the experimental results of the odor gas purifying process performed by the air purifying apparatus of the present invention configured as described above are shown in Table 1 “Odor gas purifying test”.

【0033】[0033]

【表1】 [Table 1]

【0034】表1の「臭気ガス浄化試験」は生ごみを主
原料にした堆肥工場からの排気を脱臭処理する目的で、
従来技法により建設された脱臭装置の導入ダクトにバイ
パスを設けて実施した。なお、従来法の脱臭装置は送風
装置、水洗浄装置、硫酸洗浄装置及び生分解装置などで
構成されていた。脱臭効果については本発明のものと従
来法のものとの間に殆んど差はなかったが、圧力損失及
び所要敷地面積についてはそれぞれ従来法の約40%以
下及び20%以下であった。
The "odor gas purification test" shown in Table 1 is for the purpose of deodorizing exhaust gas from a compost plant using garbage as a main raw material.
The bypass was installed in the introduction duct of the deodorizer constructed by the conventional technique. Incidentally, the deodorizing apparatus of the conventional method was composed of a blowing device, a water washing device, a sulfuric acid washing device, a biodegradation device, and the like. Although there was almost no difference between the deodorizing effect of the present invention and that of the conventional method, the pressure loss and the required site area were about 40% or less and 20% or less of the conventional method, respectively.

【0035】なお、本発明の空気浄化装置によれば、圧
力損失を大きくする活性炭、ラヒシリング等の充填材と
吸収液の循環、中和及び廃水処理などを要する苛性ソー
ダ、硫酸等の薬液などを一切必要とせず、送風装置の所
要圧力、出力、回転数は小さくなり、電気消費量及び騒
音・振動値はそれぞれ従来法よりも30%以上及び20
%以上低減し得たことなどから、装置建設費及び運転管
理を従来法の40〜50%以下に抑えられる目途を得
た。
According to the air purifying apparatus of the present invention, it is possible to completely remove the filler such as activated carbon and lahiscilling which increase the pressure loss and the chemicals such as caustic soda and sulfuric acid which require the circulation, neutralization and waste water treatment of the absorbent. Not required, the required pressure, output and rotation speed of the blower are reduced, and the electricity consumption and noise / vibration values are more than 30% and 20% lower than the conventional method, respectively.
% Or more, it is possible to reduce the equipment construction cost and operation management to 40 to 50% or less of the conventional method.

【0036】[0036]

【発明の効果】本発明は、以上に説明したように構成さ
れているので以下に記載されるような効果を奏する。
Since the present invention is configured as described above, it has the following effects.

【0037】反応部が、接ガス部を酸化チタンで被覆し
た複数の乱流通気路とその内部に装設された光照射ラン
プとからなる極めて単純な構造体なので、運転操作の簡
素化が計られる。
Since the reaction section is a very simple structure composed of a plurality of turbulent air passages in which the gas contact portion is covered with titanium oxide and a light irradiation lamp provided therein, the operation can be simplified. Can be

【0038】また、反応部を構成する複数の乱流通気路
は互に接触しないように積層された複数の波状板により
仕切られてなる空の気道状空間であり、波状板は積層両
端に位置する2枚以外は共通仕切となるために、その所
要数は有害ガスの処理に必要な乱流通気路の所要数より
も常に1単位分増えるだけであり、また波状板の所要厚
は1〜3mm程度と比較的に薄く、また共通仕切となる波
状板の表裏両面が酸化チタンで被覆されて所要総空間当
りの酸化チタン表面積を大きくするので小型軽量化が計
られるだけではなく、処理量及び乱流通気路の所要数が
大きくなる程に波状板の処理量当りの所要数及び重量の
逓減効果が高くなることから装置のスケールメリットを
大きくできる。
A plurality of turbulent air passages constituting the reaction section are empty airway-like spaces partitioned by a plurality of corrugated plates laminated so as not to contact each other. The required number is always only one unit greater than the required number of turbulent airflows required for the treatment of harmful gases, and the required thickness of the corrugated plate is 1 to Since the front and back surfaces of the corrugated plate, which is relatively thin with a thickness of about 3 mm, are coated with titanium oxide to increase the surface area of titanium oxide per required total space, not only the size and weight can be reduced, but also the processing amount and As the required number of turbulent air passages increases, the required number per corrugated plate throughput and the effect of reducing the weight increase, so that the merits of scale of the apparatus can be increased.

【0039】そして、反応部を構成する複数の乱流通気
路を流れる有害ガスが、その接ガス部に被覆された酸化
チタン面を光照射ランプで照射され、受光の瞬間に酸化
チタン面に発現する酸化チタン光触媒作用により浄化処
理されるので、ラヒシリングのような圧力損失を大きく
しガス流と光とを遮る充填材を無用となし得るから、送
風装置の所要圧力及び出力及びそれが発する騒音・振動
値を削減できるばかりではなく始動直後の最大負荷運転
をも可能し、電気消費量の節減と低公害化とが計られ
る。
Then, a harmful gas flowing through a plurality of turbulent air paths constituting the reaction section is irradiated by a light irradiation lamp on the titanium oxide surface coated on the gas contact portion, and appears on the titanium oxide surface at the moment of light reception. Since the purification treatment is performed by the titanium oxide photocatalyst, the pressure loss such as lahiscilling can be increased and the filler that blocks the gas flow and the light can be made unnecessary, so that the required pressure and output of the blower and the noise and noise generated by the same are required. Not only can the vibration value be reduced, but also maximum load operation can be performed immediately after the engine is started, reducing power consumption and reducing pollution.

【0040】さらに、反応部を構成する複数の乱流通気
路の中を流れる有害ガスが酸化チタン光触媒作用により
直接的に分解される乾式浄化処理法なので、酸やアルカ
リなどの薬液や吸収装置、中和装置及び廃水処理装置な
どを必要としないことから消耗品と装置員数との削減及
び無公害処理が可能となり、装置の建設費と運転管理費
とを節減することができる。
Furthermore, since the harmful gas flowing through the plurality of turbulent air passages constituting the reaction section is directly decomposed by the photocatalytic action of titanium oxide, it is a dry purification treatment method. Since a neutralization device and a wastewater treatment device are not required, the number of consumables and the number of devices can be reduced, and pollution-free treatment can be performed, so that the construction cost and operation management cost of the device can be reduced.

【0041】また、積層されて乱流通気路の形状を定め
る複数の波状板の波形を、三角波状、台形波状、サイン
カーブを描くうねり波状等及びそれらを適宜に組み合わ
せた多種多様な形状のものにできるので、有害ガスの処
理量、組成及び濃度などに応じて都度最適な波形の波状
板を組み合わせて千差万別な形状の乱流通気路を形成で
きるため、受光して有害ガスを浄化する酸化チタン光触
媒作用と該有害ガスの流れが接触する気−固境面の刷新
作用とを過不足なく発現させる最適な乱流が得られるこ
とから適用分野を拡大できる。
Also, the waveforms of the plurality of corrugated plates that are stacked to define the shape of the turbulent airflow path are triangular, trapezoidal, sine-curve, undulating, etc. Turbulent air passages of various shapes can be formed by combining the corrugated plates with the optimal waveform each time according to the processing amount, composition and concentration of harmful gases. An optimum turbulent flow that can express the titanium oxide photocatalytic action and the renewal action of the gas-solid interface where the flow of the harmful gas comes into contact is obtained.

【0042】さらに、乱流通気路を、波形を同じくする
も波長及び/又は振幅が規則的に変化しながら連なる形
状の波状板で形成することにより、有害ガスの浄化の進
行に伴ない逓減する濃度に順次に対応させた浄化処理が
でき、浄化効率を高めることができる。
Furthermore, by forming the turbulent airflow path with a corrugated plate having the same waveform but having a continuous shape while changing the wavelength and / or the amplitude regularly, the turbulent flow path is gradually reduced as the harmful gas purification proceeds. Purification processing can be performed sequentially according to the concentration, and purification efficiency can be increased.

【0043】また、波状板の表面に茸状、多角錐状、縦
縞状、横縞状及びそれらを適宜に組み合わせた多数の小
凸起を設けて酸化チタン光触媒作用が発現する酸化チタ
ンの被覆表面積を大きくするとともに、ガス流速に応じ
て発生する渦流で気−固境面刷新作用を発現させる乱流
の様態を律することにより、負荷変動に対する追随性を
高めることができる。
The surface of the corrugated plate is provided with a mushroom-like shape, a polygonal pyramid shape, a vertical stripe shape, a horizontal stripe shape, and a large number of small protrusions which are appropriately combined with each other. By increasing the size and controlling the turbulence in which the vortex generated according to the gas flow velocity causes the air-solid surface renewal effect, the followability to the load fluctuation can be improved.

【0044】さらに、波状板を、隣り合うもの同志が波
形、波長、振幅などを同じくするもの、波形だけを異に
するもの及び波長だけを同じくするものなどを互に接触
しないようにし且つ相互の振幅軸及び振幅位相が合致す
るように、或は相互の振幅位相が規則的なずれを持つよ
うにして積層したりすることができるので、有害ガスの
処理量、組成、濃度などに応じ最適な乱流通液路が形成
でき、処理機能の多様化を計ることができる。
Further, the corrugated plates are arranged so that adjacent ones do not contact each other with the same waveform, wavelength, amplitude, etc., those having only different waveforms, and those having only the same wavelength, and Lamination can be performed so that the amplitude axis and amplitude phase match, or the mutual amplitude and phase have regular deviations. A turbulent flow path can be formed, and diversification of processing functions can be achieved.

【0045】また、光照射ランプが透明保護体により有
害ガス流から隔離されケースの外から随時に装脱着可能
に装設され、また該光照射ランプの寿命が比較的に長く
6,000 〜9,000 時間なので、殆んどメンテナンスフリー
の長期連続運転が可能になる。
Further, the light irradiation lamp is separated from the harmful gas flow by the transparent protective body, and is mounted so as to be detachable from the outside of the case at any time, and the life of the light irradiation lamp is relatively long.
With 6,000 to 9,000 hours, almost maintenance-free long-term continuous operation is possible.

【0046】更に、光照射ランプに照度調整器及び/又
は集中監視盤に端末を接続したランプ切表示器などが設
けられるので無人運転が可能になる。
Furthermore, since the light irradiation lamp is provided with an illuminance adjuster and / or a lamp-off indicator having a terminal connected to the centralized monitoring panel, unmanned operation becomes possible.

【図面の簡単な説明】[Brief description of the drawings]

【図1】空気浄化装置の第1実施例を示す断面図であ
る。
FIG. 1 is a sectional view showing a first embodiment of an air purification device.

【図2】空気浄化装置の第2実施例を示す断面図であ
る。
FIG. 2 is a sectional view showing a second embodiment of the air purification device.

【図3】空気浄化装置の第3実施例を示す断面図であ
る。
FIG. 3 is a sectional view showing a third embodiment of the air purification device.

【図4】空気浄化装置の第4実施例を示す断面図であ
る。
FIG. 4 is a sectional view showing a fourth embodiment of the air purification device.

【符号の説明】[Explanation of symbols]

1、14、27、45 空気浄化装置 5、17、30 反応部 7、19、32、52A:52B 波状板 8、20、33、50 乱流通気路 9、21、34、53 酸化チタン面 10、23、35、54 光照射ランプ 11、24、36、55 透明保護体 22 照光群体 39 ダストチャンバ 48A 第1反応部 48B 第2反応部 51 平板 56 折返部 A 有害ガスの流れる方向を示す矢印である。 B 浄化ガスの流れる方向を示す矢印である。 C 含塵浄化ガスの流れる方向を示す矢印である。 D 1次浄化ガスの流れる方向を示す矢印である。 1, 14, 27, 45 Air purification device 5, 17, 30 Reaction unit 7, 19, 32, 52A: 52B Corrugated plate 8, 20, 33, 50 Turbulent air passage 9, 21, 34, 53 Titanium oxide surface 10 , 23, 35, 54 Light irradiation lamps 11, 24, 36, 55 Transparent protective body 22 Illumination group 39 Dust chamber 48A First reaction section 48B Second reaction section 51 Flat plate 56 Turnback section A is there. B is an arrow indicating the direction in which the purified gas flows. C is an arrow indicating the direction in which the dust-containing purified gas flows. D is an arrow indicating the direction in which the primary purification gas flows.

フロントページの続き (51)Int.Cl.6 識別記号 FI B01J 35/02 B01D 53/36 G Continued on the front page (51) Int.Cl. 6 Identification code FI B01J 35/02 B01D 53/36 G

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 主に、生物に由来する有機物質の分解や
燃焼などに伴ない発生した有害ガスを浄化する空気浄化
装置において、該有害ガスを光照射しながら無害化処理
する反応部と該反応部に該有害ガスを膨張させながら供
給する導入部とを具備し、該反応部が導入部から供給さ
れた有害ガスに乱流を与える複数の乱流通気路を備え、
該乱流通気路が複数の波状板を互に接触しないように積
層してなり、該乱流通気路の接ガス部が酸化チタンで被
覆され、該乱流通気路内に複数の光照射ランプが装設さ
れていることを特徴とする空気浄化装置。
1. An air purifying apparatus for purifying harmful gas mainly generated by decomposition and combustion of organic substances derived from living organisms, and a reaction section for detoxifying the harmful gas while irradiating the harmful gas with light. The reaction section has an introduction section that supplies the harmful gas while expanding the reaction section, and the reaction section includes a plurality of turbulent air paths that impart turbulence to the harmful gas supplied from the introduction section,
The turbulent air path is formed by laminating a plurality of corrugated plates so as not to contact each other, a gas contact portion of the turbulent air path is coated with titanium oxide, and a plurality of light irradiation lamps are provided in the turbulent air path. An air purification device characterized by being provided with.
【請求項2】 光照射ランプが透明な保護体により有害
ガスから隔離され随時装脱着可能に装設されていること
を特徴とする請求項1記載の空気浄化装置。
2. The air purifying apparatus according to claim 1, wherein the light irradiation lamp is separated from the harmful gas by a transparent protective body and is detachably mounted at any time.
JP10166207A 1998-05-29 1998-05-29 Air cleaning device Pending JPH11342317A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10166207A JPH11342317A (en) 1998-05-29 1998-05-29 Air cleaning device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10166207A JPH11342317A (en) 1998-05-29 1998-05-29 Air cleaning device

Publications (1)

Publication Number Publication Date
JPH11342317A true JPH11342317A (en) 1999-12-14

Family

ID=15827090

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10166207A Pending JPH11342317A (en) 1998-05-29 1998-05-29 Air cleaning device

Country Status (1)

Country Link
JP (1) JPH11342317A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1101909A2 (en) * 1999-11-17 2001-05-23 Volkswagen Aktiengesellschaft Photocatalytic exhaust gas purification apparatus
KR20040049587A (en) * 2002-12-06 2004-06-12 박옥현 Multi Stage Structure Photo Reacting Device For Treating Of Volatile Organic Compounds
WO2006114057A1 (en) * 2005-04-28 2006-11-02 72G Group Limited A processing module for eliminating dioxin
JP2007130042A (en) * 2005-11-08 2007-05-31 Seki:Kk Air cleaner using photocatalyst
JP2008023461A (en) * 2006-07-21 2008-02-07 Babcock Hitachi Kk Catalytic structure
WO2017069292A1 (en) * 2015-10-19 2017-04-27 주식회사 바이오메카 Air purifier using underwater bubbles
GB2551468A (en) * 2016-04-13 2017-12-27 White Gary Photocatalytic air Purifier
CN112206658A (en) * 2019-07-11 2021-01-12 赵志伟 Photocatalysis air purification filter core
WO2021035364A1 (en) * 2019-08-30 2021-03-04 Wood David J Gaseous pollution control devices and methods of removing gaseous pollutants from air
WO2022163844A1 (en) * 2021-01-29 2022-08-04 国立研究開発法人産業技術総合研究所 Air cleaning apparatus, air cleaning method, microbe removal apparatus, microbe removal method, and flow path body
CN117899647A (en) * 2024-03-18 2024-04-19 山西华丰阳化工有限公司 Spraying reaction device for formaldehyde production and operation method thereof

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1101909A2 (en) * 1999-11-17 2001-05-23 Volkswagen Aktiengesellschaft Photocatalytic exhaust gas purification apparatus
EP1101909A3 (en) * 1999-11-17 2003-06-04 Volkswagen Aktiengesellschaft Photocatalytic exhaust gas purification apparatus
KR20040049587A (en) * 2002-12-06 2004-06-12 박옥현 Multi Stage Structure Photo Reacting Device For Treating Of Volatile Organic Compounds
WO2006114057A1 (en) * 2005-04-28 2006-11-02 72G Group Limited A processing module for eliminating dioxin
JP2007130042A (en) * 2005-11-08 2007-05-31 Seki:Kk Air cleaner using photocatalyst
JP2008023461A (en) * 2006-07-21 2008-02-07 Babcock Hitachi Kk Catalytic structure
WO2017069292A1 (en) * 2015-10-19 2017-04-27 주식회사 바이오메카 Air purifier using underwater bubbles
GB2551468A (en) * 2016-04-13 2017-12-27 White Gary Photocatalytic air Purifier
GB2551468B (en) * 2016-04-13 2021-03-10 White Gary Photocatalytic air Purifier
CN112206658A (en) * 2019-07-11 2021-01-12 赵志伟 Photocatalysis air purification filter core
WO2021035364A1 (en) * 2019-08-30 2021-03-04 Wood David J Gaseous pollution control devices and methods of removing gaseous pollutants from air
WO2022163844A1 (en) * 2021-01-29 2022-08-04 国立研究開発法人産業技術総合研究所 Air cleaning apparatus, air cleaning method, microbe removal apparatus, microbe removal method, and flow path body
CN117899647A (en) * 2024-03-18 2024-04-19 山西华丰阳化工有限公司 Spraying reaction device for formaldehyde production and operation method thereof
CN117899647B (en) * 2024-03-18 2024-05-31 山西华丰阳化工有限公司 Spraying reaction device for formaldehyde production and operation method thereof

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