JP3009251B2 - Ozone treatment equipment - Google Patents
Ozone treatment equipmentInfo
- Publication number
- JP3009251B2 JP3009251B2 JP3171428A JP17142891A JP3009251B2 JP 3009251 B2 JP3009251 B2 JP 3009251B2 JP 3171428 A JP3171428 A JP 3171428A JP 17142891 A JP17142891 A JP 17142891A JP 3009251 B2 JP3009251 B2 JP 3009251B2
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- ozone generator
- gas
- blowing
- amount
- 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 - Fee Related
Links
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims description 159
- 238000011282 treatment Methods 0.000 title description 23
- 238000007664 blowing Methods 0.000 claims description 27
- 239000003054 catalyst Substances 0.000 claims description 24
- 239000003463 adsorbent Substances 0.000 claims description 23
- 230000002441 reversible effect Effects 0.000 claims description 16
- 230000003247 decreasing effect Effects 0.000 claims description 3
- 238000010926 purge Methods 0.000 claims description 3
- 229910010272 inorganic material Inorganic materials 0.000 claims 1
- 239000011147 inorganic material Substances 0.000 claims 1
- 239000007789 gas Substances 0.000 description 47
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 30
- 230000001954 sterilising effect Effects 0.000 description 19
- 238000004332 deodorization Methods 0.000 description 17
- 241000607479 Yersinia pestis Species 0.000 description 16
- 238000004659 sterilization and disinfection Methods 0.000 description 16
- 241000264877 Hippospongia communis Species 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 238000012423 maintenance Methods 0.000 description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 8
- 238000012545 processing Methods 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 6
- 239000005977 Ethylene Substances 0.000 description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 6
- -1 amine nitrates Chemical class 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- 235000013305 food Nutrition 0.000 description 6
- 241001465754 Metazoa Species 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 4
- 239000002734 clay mineral Substances 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 229910002651 NO3 Inorganic materials 0.000 description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 3
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000001877 deodorizing effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 241000251468 Actinopterygii Species 0.000 description 2
- 241001674044 Blattodea Species 0.000 description 2
- 241000255925 Diptera Species 0.000 description 2
- 241000282412 Homo Species 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 239000004113 Sepiolite Substances 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 235000015165 citric acid Nutrition 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 239000008246 gaseous mixture Substances 0.000 description 2
- 238000004255 ion exchange chromatography Methods 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 229910052624 sepiolite Inorganic materials 0.000 description 2
- 235000019355 sepiolite Nutrition 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- 241000238876 Acari Species 0.000 description 1
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical class [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 241000256602 Isoptera Species 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- 241001674048 Phthiraptera Species 0.000 description 1
- 241000258242 Siphonaptera Species 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000001339 alkali metal compounds Chemical class 0.000 description 1
- 150000001341 alkaline earth metal compounds Chemical class 0.000 description 1
- 229910001583 allophane Inorganic materials 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000003975 animal breeding Methods 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical class [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000009982 effect on human Effects 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000002070 germicidal effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 235000013980 iron oxide Nutrition 0.000 description 1
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- AMWRITDGCCNYAT-UHFFFAOYSA-L manganese oxide Inorganic materials [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 1
- PPNAOCWZXJOHFK-UHFFFAOYSA-N manganese(2+);oxygen(2-) Chemical class [O-2].[Mn+2] PPNAOCWZXJOHFK-UHFFFAOYSA-N 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000011888 snacks Nutrition 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Treating Waste Gases (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、オゾンによる処理装置
に関する。さらに詳しくは、オゾンの酸化力を利用し
て、食品工場、食品貯蔵所、製薬工場、動物飼育室、病
院、クリーンルーム、ホテル、スナック、カラオケ、一
般家庭などの脱臭、殺菌、鮮度保持、害虫の駆除などを
行う装置に関するものである。The present invention relates to an ozone treatment apparatus. In more detail, using the oxidizing power of ozone, deodorization, sterilization, freshness maintenance, pest control of food factories, food storage, pharmaceutical factories, animal breeding rooms, hospitals, clean rooms, hotels, snacks, karaoke, households The present invention relates to a device for extermination.
【0002】[0002]
【従来の技術】オゾンを用いて脱臭、殺菌する方法は、
従来から知られており、例えば、その具体的方法や実施
装置について従来から種々の提案がなされている(特開
昭54−119371号、62−57557号、63−
59961号及び実開昭63−197547号公報
等)。2. Description of the Related Art The method of deodorizing and sterilizing using ozone is as follows.
Conventionally known, for example, various proposals have been made on specific methods and implementation devices thereof (Japanese Patent Application Laid-Open Nos. 54-119371, 62-57557, 63-57).
No. 599961 and Japanese Utility Model Application Laid-Open No. 63-197747).
【0003】しかし、これらの方法では、オゾンの人
体、動物への影響があったり、操作が複雑であったり、
装置が大型であったり、処理に時間がかかったり、ある
いは脱臭や殺菌の効率が悪い等の種々の問題があった。[0003] However, in these methods, ozone has an effect on human bodies and animals, the operation is complicated,
There have been various problems such as a large device, a long processing time, and inefficient deodorization and sterilization.
【0004】[0004]
【発明が解決しようとする課題】本発明は、一つのコン
パクトな装置で、空間内の脱臭、殺菌、鮮度保持、害虫
駆除などの処理を簡便で効率よく行い、かつ人体、動
物、食品などに対して害を及ぼす残存オゾンを効率良く
分解することができる装置を提供しようとするものであ
る。DISCLOSURE OF THE INVENTION The present invention is a single compact device that performs simple and efficient treatments such as deodorization, sterilization, freshness maintenance and pest control in a space, and is applicable to human bodies, animals, foods and the like. It is an object of the present invention to provide a device capable of efficiently decomposing residual ozone that causes harm to the device.
【0005】[0005]
【課題を解決するための手段】かくして本発明によれ
ば、装置本体に気体流路を形成するための二つの開口部
が備えられ、その気体流路内に送風手段、無声放電式の
オゾン発生器、少なくともオゾンを吸着もしくは分解し
うる無機系触媒層および該オゾン発生器に供給される気
体前処理用の酸担持吸着剤層が配置され、送風手段は、
正・逆両方向に送風するための一もしくは複数のファン
と送風方向選択手段とから構成され、かつオゾン発生器
は、送風方向選択手段と連動してオゾンの発生量を調節
するための調節手段を具備することを特徴とするオゾン
による処理装置が提供される。Thus, according to the present invention, the apparatus main body is provided with two openings for forming a gas flow path, and a blowing means and a silent discharge type ozone generator are provided in the gas flow path. A device, an inorganic catalyst layer capable of adsorbing or decomposing at least ozone and an acid-carrying adsorbent layer for gas pretreatment supplied to the ozone generator are disposed,
One or a plurality of fans for blowing air in both forward and reverse directions and a blowing direction selecting means, and the ozone generator has an adjusting means for adjusting the amount of ozone generated in conjunction with the blowing direction selecting means. An ozone treatment apparatus is provided.
【0006】本発明は、二つの開口部で装置本体内に設
定される気体流路にファン、無声放電式のオゾン発生
器、オゾン吸着・分解性触媒層および該オゾン発生器に
供給される気体前処理用の酸担持吸着剤層を配置し、オ
ゾンの発生量および気体の流れ方向を変更することによ
って、一つの装置で、空間内の脱臭、殺菌、鮮度保持、
害虫の駆除などの処理と残存オゾンの分解を簡便かつ確
実に行えるよう構成したオゾンによる処理装置である。According to the present invention, a fan, a silent discharge type ozone generator, an ozone adsorbing / decomposing catalyst layer, and a gas supplied to the ozone generator are provided in a gas flow path set in the apparatus main body with two openings. By disposing an acid-carrying adsorbent layer for pretreatment and changing the amount of generated ozone and the flow direction of gas, deodorization, sterilization, freshness maintenance,
This is an ozone treatment apparatus configured so that treatment such as pest control and decomposition of residual ozone can be performed easily and reliably.
【0007】本発明の装置における送風手段は開口部と
オゾン発生器との間、オゾン発生器と無機系触媒層との
間、無機系触媒層と開口部との間のいずれに配置されて
いてもよいが、特に、気体流路内に、送風手段、オゾン
発生器、無機系触媒層の順に配置するか、オゾン発生
器、送風手段及び無機系触媒層の順で配置するのが適し
ている。酸担持吸着剤層はオゾン発生器に供給する気体
を前処理するために設置される。In the apparatus of the present invention, the air blowing means is disposed between the opening and the ozone generator, between the ozone generator and the inorganic catalyst layer, and between the inorganic catalyst layer and the opening. In particular, in the gas flow path, it is suitable to arrange the blower, the ozone generator, and the inorganic catalyst layer in this order, or to arrange the ozone generator, the blower, and the inorganic catalyst layer in this order. . The acid-carrying adsorbent layer is provided for pre-treating the gas supplied to the ozone generator.
【0008】この発明の送風手段は、正・逆両方向に送
風するための一もしくは複数のファンからなり、送風方
向選択手段を備えてなる。上記ファンは反転可能な一つ
のモーターファンで構成することができ、互いに回転方
向の異なる二つのモーターファンで構成することがで
き、これ以外に複数のモータファンで構成することもで
きる。また、送風方向選択手段は、切換スイッチ、リレ
ー等で構成することができ、その選択は自動制御するこ
とも可能である。自動制御を行う場合は、タイマーやガ
スセンサー(オゾンセンサ、においセンサ、エチレンセ
ンサ等)等がさらに備えられ、これに選択手段が連動す
るよう構成される。この連動は、通常の制御回路で実現
できる。なお、この際のタイマーやガスセンサは装置本
体に付設しておくのが好ましい。但し、これらタイマー
やガスセンサは必ずしも連動してなくてもよく、一つの
報知手段であってもよい。[0008] The blowing means of the present invention comprises one or a plurality of fans for blowing in both forward and reverse directions, and comprises blowing direction selecting means. The fan may be configured with one reversible motor fan, may be configured with two motor fans having different rotation directions from each other, and may be configured with a plurality of motor fans. Further, the blowing direction selecting means can be constituted by a changeover switch, a relay or the like, and the selection can be automatically controlled. In the case of performing automatic control, a timer, a gas sensor (an ozone sensor, an odor sensor, an ethylene sensor, etc.) are further provided, and the selecting means is configured to operate in conjunction therewith. This interlock can be realized by a normal control circuit. In this case, it is preferable that the timer and the gas sensor are attached to the apparatus main body. However, these timers and gas sensors do not necessarily have to be linked, and may be one notification means.
【0009】本発明における無声放電式のオゾン発生器
には、上記送風方向選択手段と連動してオゾン発生量を
調節する調節手段が具備される。ここで「連動」とは、
送風方向選択手段によって正(又は逆)方向の送風が選
択された際、オゾン発生器のオゾンの発生量を最大側に
設定し、一方送風方向選択手段によって逆(又は正)方
向の送風が選択された際オゾン発生器のオゾンの発生量
を減少側ないし停止側に設定することを意味する。より
具体的には、上記調節手段には、送風方向が、無機系触
媒層からオゾン発生器への方向(正方向)の際に、オゾ
ン発生器のオゾン発生量を最大側に設定し、オゾン発生
器から無機系触媒層への方向(逆方向)の際に、オゾン
発生器のオゾン発生量を減少側(又は停止側)に切換設
定する手段か、又はこれと逆の制御を行う手段が含まれ
る。The silent discharge type ozone generator according to the present invention is provided with adjusting means for adjusting the amount of ozone generated in conjunction with the blowing direction selecting means. Here, “interlock” means
When forward (or reverse) airflow is selected by the airflow direction selection means, the amount of ozone generated by the ozone generator is set to the maximum side, while airflow in the reverse (or forward) direction is selected by the airflow direction selection means. Means that the ozone generation amount of the ozone generator is set to a decreasing side or a stopping side. More specifically, when the blowing direction is the direction (positive direction) from the inorganic catalyst layer to the ozone generator, the amount of ozone generated by the ozone generator is set to the maximum side. In the direction (reverse direction) from the generator to the inorganic catalyst layer, the means for switching and setting the ozone generation amount of the ozone generator to the decreasing side (or the stop side), or the means for performing the reverse control is used. included.
【0010】かかるオゾン発生器の調節手段は、無声放
電式のオゾン発生器の種類によって異なるが、前記選択
手段のモードに対応して作動するON−OFF切換スイ
ッチ、高出力−低出力切換スイッチ等の切換手段によっ
て構成できる。この発明における酸担持吸着剤層は、上
記無声放電式オゾン発生器に供給する気体、通常被処理
ガスの一部または大気を前処理するために設けられる。
ことにかかる酸担持吸着剤層は、被処理ガスの一部また
は大気に含まれる、アンモニア,アミン類を除去し、無
声放電式オゾン発生器における電極表面でのアンモニ
ア,アミン類の硝酸塩,亜硝酸塩の発生沈積を防止又は
抑制してオゾン発生効率の安定化に役立つものである。
なお、送風方向選択手段などによって、オゾン発生量が
停止側に設定された場合、オゾン発生器の電極に供給す
る気体で該電極内をパージすることによって、オゾン発
生器の電極の前後の配管、機器、その他をオゾンガスに
よる腐食劣化からさけることができるので、このパージ
は、この発明の好ましい態様である。Although the adjusting means of the ozone generator differs depending on the type of the silent discharge type ozone generator, an ON-OFF switch, a high output-low output switch, etc., which operates in accordance with the mode of the selecting means. Can be constituted by the switching means. The acid-carrying adsorbent layer in the present invention is provided for pretreating a gas supplied to the silent discharge type ozone generator, usually a part of the gas to be treated or the atmosphere.
In particular, the acid-supporting adsorbent layer removes ammonia and amines contained in a part of the gas to be treated or in the air, and forms ammonia, amine nitrates and nitrite on the electrode surface in a silent discharge ozone generator. It is useful for stabilizing ozone generation efficiency by preventing or suppressing generation and deposition of ozone.
When the ozone generation amount is set to the stop side by the blowing direction selection means or the like, by purging the inside of the electrode with the gas supplied to the electrode of the ozone generator, piping before and after the electrode of the ozone generator, This purging is a preferred embodiment of the present invention because the equipment, etc., can be protected from corrosion degradation by ozone gas.
【0011】かかる酸担持吸着剤としては、たとえば、
硫酸、リン酸などの無機酸、たとえばシュウ酸、クエン
酸、リンゴ酸などの有機酸を活性炭(BET比表面積2
00〜2500m2/g)、またはアロフェン、珪藻
土、頁岩、沸石、セピオライト、活性白土などの粘土鉱
物(焼成したものを含む)および活性炭とこれら粘土鉱
物との混合物に担持したものが挙げられる。As such an acid-carrying adsorbent, for example,
An inorganic acid such as sulfuric acid or phosphoric acid, for example, an organic acid such as oxalic acid, citric acid or malic acid is converted into activated carbon (BET specific surface area 2
00-2500 m 2 / g) or clay minerals (including calcined ones) such as allophane, diatomaceous earth, shale, zeolite, sepiolite and activated clay, and those supported on a mixture of activated carbon and these clay minerals.
【0012】酸担持吸着剤層の形状としては、ペレット
状、顆粒状、多孔板状、板状、マカロニ状、ハニカム
状、繊維状などが挙げられ、特に顆粒状、ハニカム状、
繊維状が好ましい。吸着剤への酸の担持量は2〜50w
t%が適しており、5〜40wt%が好ましい。Examples of the shape of the acid-supporting adsorbent layer include pellets, granules, perforated plates, plates, macaroni, honeycombs, and fibers.
Fibrous is preferred. The amount of acid carried on the adsorbent is 2 to 50 w
t% is suitable, and 5 to 40 wt% is preferable.
【0013】特に、硫酸、リン酸またはクエン酸を比表
面積500〜2000m2/gのペレット状、ハニカム
状、繊維状の活性炭(活性炭を主体とした粘土鉱物との
混合物を含む)に5〜40wt%担持したものが最も好
ましい。酸を担持せしめる方法としては、吸着剤に酸水
溶液を散布する方法、吸着剤を酸水溶液に浸して含浸す
る方法、活性炭と粘土鉱物を吸着剤とする場合は成型す
る前に酸水溶液を混練し、担持する方法などが挙げられ
る。担持後、必要に応じて乾燥する。In particular, sulfuric acid, phosphoric acid, or citric acid is added to a pellet, honeycomb, or fibrous activated carbon having a specific surface area of 500 to 2,000 m 2 / g in an amount of 5 to 40 wt. % Is most preferred. As a method of supporting an acid, a method of spraying an acid aqueous solution on an adsorbent, a method of immersing the adsorbent in an acid aqueous solution, and impregnating the activated carbon and clay mineral as an adsorbent, knead the acid aqueous solution before molding. And a method of carrying. After loading, drying is performed as necessary.
【0014】被処理ガスの一部または大気を酸担持吸着
剤に接触させる際の温度は0〜100°C、好ましくは
5〜80°Cで、酸担持吸着剤に対するガスの空間速度
は100〜500,000hr-1、好ましくは500〜
100,000hr-1である。被処理ガスの一部または
大気を酸担持吸着剤に接触させることによって、前述の
ごとく該ガスの種々の微量成分が除去される。特に塩基
性を呈するアンモニア、アミン類などは選択的に除去さ
れ、オゾン発生電極表面での硝酸塩の副生などが抑えら
れ、オゾン発生効率を安定化できると考えられる。The temperature at which a part of the gas to be treated or the atmosphere is brought into contact with the acid-carrying adsorbent is 0 to 100 ° C., preferably 5 to 80 ° C., and the space velocity of the gas with respect to the acid-carrying adsorbent is 100 to 100 ° C. 500,000 hr -1 , preferably 500 to
100,000 hr -1 . By bringing a part of the gas to be treated or the atmosphere into contact with the acid-carrying adsorbent, various trace components of the gas are removed as described above. In particular, it is considered that ammonia, amines, and the like exhibiting basicity are selectively removed, the by-product of nitrate on the surface of the ozone generation electrode is suppressed, and the ozone generation efficiency can be stabilized.
【0015】なお、被処理ガスの一部または大気を酸担
持吸着剤に接触させるに先立って、先ず活性炭(比表面
積500〜3000m2/g)に接触させて、炭化水
素、アルデヒド類、カルボン酸類、イオウ化合物などの
微量多成分を予め除去するよう構成しておくことは、オ
ゾン発生効率を一層向上させる上で重要である。この発
明における無機系触媒層は、オゾンを吸着もしくは分解
しうる通気可能なものであればよく、さらに、オゾンの
存在下で、脱臭、殺菌作用を促進できるものが好まし
い。この具体例としては、例えば、活性炭、アルミナ、
シリカ、コージエライト、セピオライト、ゼオライト、
粘土鉱物、チタニア、ジルコニア、マグネシア、鉄酸化
物、銅酸化物、マンガン酸化物、コバルト酸化物などの
単独およびこれらの混合物が挙げられる。また、これら
単独品および混合物にさらにアルカリ金属化合物、アル
カリ土類金属化合物、白金族化合物などを添加または担
持させたものでもよい。特に、活性炭系のものは、本装
置でのオゾン処理効率を向上させる上で適している。な
お、この無機系触媒層との接触処理は、粒状の上記無機
系触媒層の充 層や上記繊維状、ハニカム状、多孔板状
等のフィルター等の形状のものに被処理気体を通過させ
ることにより行うことができ、フィルターを用いるのが
好ましい。特にハニカム状フィルターは圧損が小さく、
気体の流れが均一となるため、最も好ましい。この際こ
れらフィルターは、一種類でも良いが、場合によって
は、二種類以上のフィルターを適当に組合わせて、脱臭
効果、殺菌効率やオゾン分解効率を向上させることもで
きる。Prior to contacting a part of the gas to be treated or the atmosphere with the acid-carrying adsorbent, the gas is first brought into contact with activated carbon (specific surface area: 500 to 3000 m 2 / g) to obtain hydrocarbons, aldehydes and carboxylic acids. It is important to previously remove trace multi-components such as sulfur compounds in order to further improve the ozone generation efficiency. The inorganic catalyst layer in the present invention may be any layer capable of adsorbing or decomposing ozone and capable of aeration, and more preferably a layer capable of promoting deodorization and sterilization in the presence of ozone. Specific examples of this include, for example, activated carbon, alumina,
Silica, cordierite, sepiolite, zeolite,
Clay minerals, titania, zirconia, magnesia, iron oxides, copper oxides, manganese oxides, cobalt oxides, etc., alone and in mixtures thereof. In addition, an alkali metal compound, an alkaline earth metal compound, a platinum group compound, or the like may be added to or supported on a single product or a mixture thereof. In particular, the activated carbon type is suitable for improving the ozone treatment efficiency in the present apparatus. The contact treatment with the inorganic catalyst layer is performed by passing the gas to be treated through a granular filler layer of the inorganic catalyst layer or a filter such as a fibrous, honeycomb, or perforated plate. And a filter is preferably used. In particular, honeycomb filters have low pressure loss,
This is most preferable because the gas flow becomes uniform. In this case, one kind of these filters may be used, but in some cases, two or more kinds of filters may be appropriately combined to improve the deodorizing effect, the sterilizing efficiency, and the ozone decomposing efficiency.
【0016】この発明の装置を駆動するに際し、オゾン
の処理条件は悪臭成分、菌、害虫、空間の種類などによ
って異なるが、例えば、オゾン発生量とファンの風量
は、オゾン濃度が0.1〜10,000ppm、好まし
くは、0.2〜5,000ppm、より好ましくは0.
4〜2,500ppmの範囲内となるように調整するの
が良く、オゾン処理時間(オゾン放出時間)は1分以
上、好ましくは5分以上が良く、処理温度は、−50〜
100°C好ましくは、−30〜70°Cが良い。When the apparatus of the present invention is driven, the ozone treatment conditions vary depending on the odorous components, bacteria, pests, the type of space, and the like. 10,000 ppm, preferably 0.2 to 5,000 ppm, more preferably 0.1 ppm.
It is preferable to adjust so as to be within the range of 4 to 2,500 ppm, the ozone treatment time (ozone release time) is 1 minute or more, preferably 5 minutes or more, and the treatment temperature is -50 to
100 ° C, preferably -30 to 70 ° C.
【0017】[0017]
【作用】送風方向の切換とオゾン発生のON−OFF又
はその発生量の大−小の切換が連動して行われるため、
送風方向の切換を行うことにより、例えばオゾン放出に
よる脱臭、殺菌、鮮度保持、害虫駆除を主とする処理
と、オゾンの無機系触媒層による吸着・分解除去を主と
する処理とを、状況に応じて一台の装置によって選択し
て行うことができることとなる。The switching of the blowing direction and the ON / OFF of ozone generation or the switching of the amount of ozone generation are performed in conjunction with each other.
By switching the blowing direction, for example, processing mainly on deodorization by ozone release, sterilization, keeping freshness, extermination of insect pests, and processing mainly on adsorption and decomposition removal of ozone by the inorganic catalyst layer can be changed to the situation. This can be selectively performed by one device in response.
【0018】そして、この際酸担持吸着剤層が、オゾン
放出による脱臭、殺菌、鮮度保持、害虫の駆除時に被処
理ガス中の微量成分のオゾン発生器の電極面への悪影響
を防止又は抑制してオゾン処理効率をより向上するよう
作用し、オゾン発生器停止時には系内の腐食等を防止す
るよう作用する。従って、かかる本発明の装置によれ
ば、一台の装置で脱臭、殺菌、鮮度保持、害虫駆除処理
とその後の後処理を効率良く安定に行うことが可能とな
る。ここで害虫とは、ゴキブリ,ダニ,白アリ,ノミ,
シラミ,蝿,蚊などの家屋害虫や不快害虫と称されるも
のである。At this time, the acid-carrying adsorbent layer prevents or suppresses the adverse effects of trace components in the gas to be treated on the electrode surface of the ozone generator during deodorization, sterilization, freshness maintenance and pest control by ozone release. Thus, it works to further improve the ozone treatment efficiency, and when the ozone generator is stopped, it works to prevent corrosion and the like in the system. Therefore, according to the apparatus of the present invention, deodorization, sterilization, freshness maintenance, pest control and subsequent post-processing can be efficiently and stably performed by one apparatus. Here, pests include cockroaches, mites, termites, fleas,
House pests such as lice, flies, and mosquitoes are also referred to as unpleasant pests.
【0019】[0019]
【実施例】以下本発明を実施例により、さらに詳細に説
明する。まず第1図は、本発明の一実施例の処理装置
(7A)を示すものであり、箱体状の気体流路(149
0cm3)に、一方の開口部1、活性炭ハニカムからな
る無機系触媒層3、無声放電式オゾン発生器4、オゾン
発生電極に供給する気体の一部を処理する酸担持吸収剤
層5(H3PO4−30%担持活性炭ペレット)、反転可
能なファン6、他方の開口部2がこの順に配置されてい
る。そして、ファン6にはON−OFFスイッチ以外に
その送風方向を切換えられるように タイマーによる切
換スイッチ(図示せず)が付設されており、さらにこの
切換スイッチの選択により、送風方向は図面の左から右
となったときに、オゾン発生器の出力を最大(周波数
1.8kHz,電圧7.0KVpp)となるように設定
し、逆に送風方向が右から左となったときに、オゾン発
生器の出力がゼロ(停止)にするスイッチング制御回路
からなるオゾン発生量調節手段(図示せず)が備えられ
ている。また、第3図は、オゾン処理すべき空間8とオ
ゾン処理装置7Aとの関係を示す概略図である。The present invention will be described in more detail with reference to the following examples. First, FIG. 1 shows a processing apparatus (7A) according to an embodiment of the present invention, which has a box-shaped gas flow path (149).
0 cm 3 ), one opening 1, an inorganic catalyst layer 3 made of activated carbon honeycomb, a silent discharge type ozone generator 4, and an acid-carrying absorbent layer 5 (H) for treating a part of gas supplied to an ozone generation electrode. 3 PO 4 -30% -supported activated carbon pellets), a reversible fan 6 and the other opening 2 are arranged in this order. In addition to the ON-OFF switch, the fan 6 is provided with a changeover switch (not shown) using a timer so that the airflow direction can be changed. Further, by selecting this changeover switch, the airflow direction is changed from the left of the drawing. When the output becomes right, the output of the ozone generator is set to the maximum (frequency: 1.8 kHz, voltage: 7.0 KVpp). Conversely, when the blowing direction changes from right to left, the output of the ozone generator is changed. An ozone generation amount adjusting means (not shown) including a switching control circuit for making the output zero (stop) is provided. FIG. 3 is a schematic diagram showing the relationship between the space 8 to be subjected to ozone treatment and the ozone treatment device 7A.
【0020】かかる処理装置7A(第1図)の駆動及び
機能について説明する。まず、気体が開口部1から開
口部2へ流れるようにファン6の回転方向をセットす
る。この際にはオゾン発生量が最大となるようにオゾン
発生器4が設定され、吸引気体とオゾンとがファン6で
均一に混合され開口部2から該混合気体が放出される。
これにより、高濃度のオゾンが空間内に拡散し、空間内
の悪臭成分、浮遊菌、エチレンなどとオゾンが反応し、
また空間内に存在する食品類、付着菌、害虫などにもオ
ゾンが作用して、脱臭、殺菌、鮮度保持、害虫の駆除な
どの効果を発揮する。また、オゾン発生器に流通するガ
スは酸担持吸着剤層5で処理されているため、オゾン発
生器4の電極面の劣化が著しく制御される。The drive and function of the processing device 7A (FIG. 1) will be described. First, the rotation direction of the fan 6 is set so that the gas flows from the opening 1 to the opening 2. At this time, the ozone generator 4 is set so that the amount of generated ozone is maximized, the suction gas and ozone are uniformly mixed by the fan 6, and the mixed gas is discharged from the opening 2.
As a result, high-concentration ozone diffuses into the space, and the ozone reacts with odorous components, floating bacteria, ethylene, etc. in the space,
In addition, ozone acts on foods, attached bacteria, pests, and the like existing in the space, and exerts effects such as deodorization, sterilization, freshness maintenance, and pest control. Further, since the gas flowing through the ozone generator is treated by the acid-carrying adsorbent layer 5, deterioration of the electrode surface of the ozone generator 4 is significantly controlled.
【0021】この際、ファンで吸引される気体には、未
反応で残存する悪臭成分、エチレン、浮遊菌、オゾンな
どが含まれ、これらは、開口部1を経由して触媒層3に
接触して、それぞれ効率よく分解され、脱臭、殺菌、鮮
度保持の効果を一層向上させる。触媒層3を通過した気
体は、前述したようにオゾンと再混合され、再び空間へ
拡散していく。この操作を一定時間続けることによって
空間内のオゾン濃度は、ほぼ一定となり、脱臭、殺菌、
鮮度保持、害虫の駆除の作用が継続する。At this time, the gas sucked by the fan contains unreacted unpleasant odor components, ethylene, floating bacteria, ozone, etc., which come into contact with the catalyst layer 3 through the opening 1. Thus, they are efficiently decomposed, and the effects of deodorization, sterilization, and freshness maintenance are further improved. The gas that has passed through the catalyst layer 3 is remixed with ozone as described above, and diffuses again into the space. By continuing this operation for a certain period of time, the ozone concentration in the space becomes almost constant, deodorizing, sterilizing,
The effect of maintaining freshness and controlling pests continues.
【0022】一方、ファンの回転方向を逆にして、気
体を開口部2から開口部1へ流れるようにする。この際
には、オゾン発生量がゼロとなるようにオゾン発生器4
が設定される。これにより吸引気体が触媒層3を通過
し、未反応の余剰オゾンが完全に分解され、人体、動物
などに害を及ぼすことがなくなる。そして、このような
との操作および/または装置全体の停止をタイマー
やオゾンセンサー9などで制御することによって自動的
に脱臭、殺菌、鮮度保持、害虫の駆除などのオゾン処理
が容易にできる。また,操作および/または装置の
停止を繰り返すこともできる。この自動制御は、装置本
体に付設されたタイマーによる所定の周期毎に、あるい
はオゾンセンサの出力の大小に基づいて、前記したファ
ン6の送風方向選択手段を切換えるよう構成して行うこ
とができる。On the other hand, the direction of rotation of the fan is reversed so that gas flows from the opening 2 to the opening 1. At this time, the ozone generator 4 is set so that the ozone generation amount becomes zero.
Is set. As a result, the suctioned gas passes through the catalyst layer 3, and the unreacted surplus ozone is completely decomposed, so that no harm is caused to humans, animals, and the like. By controlling such operations and / or stopping the entire apparatus with a timer, an ozone sensor 9, or the like, ozone treatment such as deodorization, sterilization, freshness maintenance, and pest control can be easily performed easily. Also, the operation and / or the stopping of the device can be repeated. This automatic control can be performed by switching the air flow direction selection means of the fan 6 at predetermined intervals by a timer attached to the apparatus main body or based on the magnitude of the output of the ozone sensor.
【0023】一方、第2図は、本発明の他の実施例の処
理装置7Bを示すものであり、箱体状の気体流路(23
920cm3)に一方の開口部1、5wt%の炭酸カリ
ウムを担持した活性炭ハニカムからなる無機系触媒層
3、反転可能なファン6、オゾン発生器4、オゾン発生
器に供給する気体を処理する酸担持吸着剤層5(H2S
O4−10wt%担持活性炭ハニカム)、他方の開口部
2がこの順にはいちされている。なお、10はオゾン発
生器に気体を供給するためのエアーポンプである。FIG. 2 shows a processing apparatus 7B according to another embodiment of the present invention.
920 cm 3 ) One opening 1, inorganic catalyst layer 3 made of activated carbon honeycomb supporting 5 wt% potassium carbonate, reversible fan 6, ozone generator 4, acid for treating gas supplied to ozone generator Supported adsorbent layer 5 (H 2 S
O 4 -10 wt% carrying activated carbon honeycomb), and the other opening 2 is formed in this order. Reference numeral 10 denotes an air pump for supplying gas to the ozone generator.
【0024】そして、ファン6にはON−OFFスイッ
チ以外にその送風方向を切換える切換スイッチ(図示せ
ず)が付設されており、さらにこの切換スイッチの選択
により、送風方向が図面の右→左となったときに、オゾ
ン発生器の出力を最大(周波数11.76KHz、電圧
8.4KVpp)にするスイッチング制御回路からなる
オゾン発生量調節手段(図示せず)が備えられている。In addition to the ON-OFF switch, the fan 6 is provided with a changeover switch (not shown) for changing the air blowing direction. Further, by selecting this changeover switch, the air blowing direction changes from right to left in the drawing. When this happens, an ozone generation amount adjusting means (not shown) comprising a switching control circuit for maximizing the output of the ozone generator (frequency: 11.76 KHz, voltage: 8.4 KVpp) is provided.
【0025】かかる処理装置7Bの駆動及び機能につい
て説明する。まず、気体が開口部1から開口部2へ流
れるようにファン6の回転方向をセットすることによ
り、オゾン発生量が最小となるようにオゾン発生器4が
設定され、吸引気体とオゾンとが混合され開口部2から
該混合気体が放出され、比較的に低濃度のオゾンが空間
内に拡散し、空間内の悪臭成分、浮遊菌、エチレンなど
とオゾンが反応し、かつこの混合気体を触媒層に流通す
ることによって脱臭、殺菌鮮度保持などの作用を呈す
る。この空間でのオゾン濃度は比較的に低くなるので人
体、動物、食品などに対して害のないような雰囲気に保
たれることとなる。The drive and function of the processing device 7B will be described. First, by setting the rotation direction of the fan 6 so that the gas flows from the opening 1 to the opening 2, the ozone generator 4 is set so that the amount of generated ozone is minimized. The gaseous mixture is released from the opening 2, and a relatively low concentration of ozone diffuses into the space, and the ozone reacts with malodorous components, airborne bacteria, ethylene, etc. in the space, and the gaseous mixture is converted into a catalyst layer. By distributing to, it exhibits effects such as deodorization and sterilization freshness maintenance. Since the ozone concentration in this space is relatively low, the atmosphere is kept harmless to humans, animals, foods and the like.
【0026】一方、ファンの回転方向を逆にして、気
体が開口部2から開口部1へ流れるようにすることによ
りオゾン発生量が最大となるように設定され、これによ
り吸引気体とオゾンとをファン6で混合して触媒層に均
一に流通させることによって、吸引気体中の悪臭成分、
浮遊菌、エチレンをオゾンで酸化分解し、脱臭、殺菌、
鮮度保持などの作用が効率よくかつ安定に発揮され、か
つオゾンも触媒層でほぼ完全に分解され、洗浄な気体と
なって、開口部1から空間へ出て行く。On the other hand, the direction of rotation of the fan is reversed so that gas flows from the opening 2 to the opening 1, so that the amount of generated ozone is set to be maximum. By mixing with the fan 6 and uniformly flowing through the catalyst layer, malodorous components in the suction gas,
Oxidation and decomposition of airborne bacteria and ethylene with ozone, deodorization, sterilization,
The effect of maintaining freshness and the like is efficiently and stably exhibited, and ozone is almost completely decomposed in the catalyst layer to become a clean gas and exits from the opening 1 into the space.
【0027】このとおよび/または装置の停止の操
作または,および/または装置の停止の繰返しの操
作も前記と同様にタイマー、オゾンセンサー9などで制
御できる。 実施例1 鮮魚および肉類を解体し、パック包装する容積100m
3の部屋の中央にオゾン発生能力1,000mg/H
(露点−72°Cの空気での能力)のオゾン発生器,B
ET表面積1,200m2/gの活性炭ハニカム(セル
数300個/m2、サイズ84mm×44mm×20m
m)100枚を搭載した第4図に示すごとき本発明のオ
ゾン処理装置を設置し、魚臭および肉臭実験を行った。
この装置には、オゾン発生器の電極に20l/minの
ガスを通気するためのエアポンプと、工程を進めるため
の二つのタイマーが付設されている。図中、11は活性
炭ハニカムからなる無機系触媒層、12は無声放電式オ
ゾン発生器、13はエアーポンプ、14は酸担持吸着剤
層、15は反転可能なファンを各々示すものである。This operation and / or the operation of stopping the apparatus and / or the operation of repeatedly stopping the apparatus can be controlled by the timer, the ozone sensor 9 and the like in the same manner as described above. Example 1 A volume of 100 m for disassembling fresh fish and meat and packing them in packs
Ozone generation capacity 1,000mg / H in the center of room 3
Ozone generator (capacity in air with dew point -72 ° C), B
Activated carbon honeycomb with an ET surface area of 1,200 m 2 / g (300 cells / m 2 , size 84 mm × 44 mm × 20 m
m) The ozone treatment apparatus of the present invention as shown in FIG. 4 equipped with 100 sheets was installed, and fish odor and meat odor experiments were performed.
The apparatus is provided with an air pump for passing gas at 20 l / min to the electrode of the ozone generator and two timers for proceeding the process. In the figure, 11 denotes an inorganic catalyst layer made of activated carbon honeycomb, 12 denotes a silent discharge type ozone generator, 13 denotes an air pump, 14 denotes an acid-carrying adsorbent layer, and 15 denotes a reversible fan.
【0028】装置本体のスイッチをONにすると第1タ
イマーがONとなり、第1工程が行われ、第1タイマー
の設定時間が経過すると、第1タイマーがOFFとなり
同時に第2タイマーがONとなり、第2工程が行われ、
第2タイマーの設定時間が経過すると第2タイマーがO
FFとなり装置本体が停止するように設計されている。When the switch of the apparatus main body is turned on, the first timer is turned on, the first step is performed, and when the set time of the first timer elapses, the first timer is turned off, and at the same time, the second timer is turned on. Two steps are performed,
When the set time of the second timer elapses, the second timer becomes O
It is designed so that it becomes an FF and the device body stops.
【0029】二つのタイマーの作動と工程との関係はつ
ぎの通りである。The relationship between the operation of the two timers and the process is as follows.
【0030】[0030]
【表1】 [Table 1]
【0031】第1タイマーおよび第2タイマーの設定時
間をそれぞれ5時間および2時間として、次のような二
つの実験を行った。 <実験−1>オゾン発生器の電極面に通気するガスの前
処理なし(比較例) この部屋での通常の作業を終えた後、部屋をほぼ密閉状
態にして装置本体のスイッチをONにして作動を開始し
た。部屋中央附近のオゾン濃度をオゾンモニターで調べ
た結果を第1表に示す。The following two experiments were conducted with the set times of the first timer and the second timer set to 5 hours and 2 hours, respectively. <Experiment-1> No pretreatment of gas passing through the electrode surface of the ozone generator (Comparative Example) After normal work in this room was completed, the room was almost closed, and the switch of the device body was turned ON. Operation started. Table 1 shows the results of an ozone monitor study of the ozone concentration near the center of the room.
【0032】実験開始から7時間経過後、部屋内のオゾ
ン濃度は、0ppmとなっており、モニター5人が部屋
に入り官能テストを行ったが、装置運転の前後で大差な
く、脱臭されていなかった。実施後、オゾン発生器の電
極を水で洗浄し、イオンクロマトグラフィで調べたとこ
ろ、かなりの量の硝酸イオンが検出された。すなわち、
部屋の内に存在していたアンモニア、トリメチルアミン
(合計して、約1.5ppm)が、オゾン発生器内で生
成する窒素酸化物(主にN2O5)と反応し、電極面に硝
酸塩の結晶が付着し、オゾン発生が著しく抑制され、オ
ゾンによる脱臭がうまくいかなかった。 <実験−2>BET表面積1500m2/gの4〜6メ
ッシュ粒状活性炭にリン酸25wt%添着したものを1
00mmφのカラムに800ml充填して、酸担持吸着剤
層としこれにオゾン発生器に通気するガスを流し前処理
する(本発明)前記実験−1の1週間後に、実験−1と
同じように実験を行った。部屋内のオゾン濃度の経時変
化を同じ第1表に示した。実験開始7時間後、部屋内の
オゾン濃度は0ppmとなっており、モニター5人全員
が良く脱臭されていることを確認した。Seven hours after the start of the experiment, the ozone concentration in the room was 0 ppm, and five monitors entered the room and performed a sensory test. Was. After the implementation, the electrodes of the ozone generator were washed with water and examined by ion chromatography. As a result, a considerable amount of nitrate ions was detected. That is,
Ammonia and trimethylamine (approximately 1.5 ppm in total) that existed in the room react with nitrogen oxides (mainly N 2 O 5 ) generated in the ozone generator, and nitrate on the electrode surface is formed. Crystals adhered, the generation of ozone was significantly suppressed, and deodorization with ozone was not successful. <Experiment-2> 4 to 6 mesh granular activated carbon having a BET surface area of 1500 m 2 / g and 25% by weight of phosphoric acid impregnated with 1
A column having a diameter of 00 mm is filled with 800 ml to form an acid-supporting adsorbent layer, which is then subjected to pretreatment by flowing gas passing through an ozone generator (invention). One week after the above-mentioned experiment-1, an experiment was conducted in the same manner as experiment-1. Was done. Table 1 shows the changes over time in the ozone concentration in the room. Seven hours after the start of the experiment, the ozone concentration in the room was 0 ppm, and it was confirmed that all five monitors were well deodorized.
【0033】テスト後、実験−1と同じようにオゾン発
生器の電極を水で洗浄し、イオンクロマトグラフィで調
べたが、硝酸イオンは検出されなかった。第1表からオ
ゾン発生器に通気するガスを、酸担持吸着剤層で前処理
することによって、オゾン発生効率が常に高く維持さ
れ、オゾンの脱臭効率が著しく向上されることがわか
る。After the test, the electrode of the ozone generator was washed with water and examined by ion chromatography in the same manner as in Experiment 1, but no nitrate ion was detected. From Table 1, it can be seen that by pre-treating the gas passing through the ozone generator with the acid-carrying adsorbent layer, the ozone generation efficiency is always kept high, and the ozone deodorization efficiency is significantly improved.
【0034】[0034]
【表2】 [Table 2]
【0035】実施例2 内容積25m3のオフィスの1室(室内温度:24.5
°C)に、体長約8.5mmのゴキブリ6匹を入れ、こ
の室に無声放電方式のオゾン発生器(オゾン発生量50
0mg/hr)とファン(風量2.1m3/min)と
を搭載したオゾン放散機を置き、密閉状態で1.5pp
mのオゾンを含有する大気(温度:25.8°C)を1
26m3/hrで1時間循環した。Example 2 One room of an office having an internal volume of 25 m 3 (indoor temperature: 24.5)
° C), six cockroaches having a body length of about 8.5 mm were put in the chamber, and a silent discharge type ozone generator (ozone generation amount 50
0 mg / hr) and an ozone diffuser equipped with a fan (air volume: 2.1 m 3 / min) and 1.5 pp in a closed state.
m atmosphere of ozone (temperature: 25.8 ° C)
Circulation was performed at 26 m 3 / hr for 1 hour.
【0036】オゾン放散開始から約40分後に、室内の
オゾン濃度は1.05ppmに達し、ほぼ平衡状態(室
内温度:25.5°C)となっていた。オゾン含有ガス
の放散終了後6時間後に、断面積1,850cm2の活
性炭ハニカム(セル数:300/inch2;厚さ:2
0mm)に室内の空気を2.1m3/hrで流通循環し
た。流通後30分後に、オゾンの濃度は0.05ppm
以下になった。About 40 minutes after the start of ozone emission, the ozone concentration in the room reached 1.05 ppm and was almost in an equilibrium state (room temperature: 25.5 ° C.). Six hours after the end of the release of the ozone-containing gas, an activated carbon honeycomb having a cross-sectional area of 1,850 cm 2 (number of cells: 300 / inch 2 ; thickness: 2)
(0 mm), the room air was circulated at 2.1 m 3 / hr. 30 minutes after distribution, the concentration of ozone is 0.05 ppm
It became the following.
【0037】室のドアを開け、室内を観察したところ、
4匹が床の上で仰向きになり死んだ状態で、残る2匹は
かなり衰弱していた。When the door of the room was opened and the room was observed,
Four were dead and lying on the floor, while the other two were quite weak.
【0038】[0038]
【発明の効果】オゾンは、酸化力が強く、脱臭、殺菌、
鮮度保持、、害虫の駆除などの広範囲の作用を示す。オ
ゾンによる主要悪臭成分の酸化反応を示すと以下のよう
になると考えられる。As described above, ozone has a strong oxidizing power, and is deodorized, sterilized,
It has a wide range of effects such as maintaining freshness and controlling pests. It is considered that the oxidation reaction of the main malodorous component by ozone is as follows.
【0039】H2S→S,CH3SH→CH3SOSC
H3,H 2 S → S, CH 3 SH → CH 3 SOSC
H 3 ,
【化1】 (CH3)3N→CH3NO2,NH3→NH4NO3 オゾンによる殺菌は、オゾンが菌の細胞壁または細胞膜
に作用し、破壊または分解することによると考えられ、
他の殺菌性ガスよりも処理が容易で残留性がない。オゾ
ンによる食品類の鮮度保持は前記の殺菌作用によるもの
と野菜、果物などの植物の成熟老化を促進するエチレン
を酸化分解するものとがある。Embedded image (CH 3 ) 3 N → CH 3 NO 2 , NH 3 → NH 4 NO 3 Sterilization by ozone is considered to be caused by ozone acting on cell walls or cell membranes of bacteria, and destroying or decomposing them.
Easier to process and less persistent than other germicidal gases. The preservation of the freshness of foods by ozone is based on the above-mentioned bactericidal action or on the oxidative decomposition of ethylene which promotes the mature aging of plants such as vegetables and fruits.
【0040】一方、未反応のオゾンは触媒体表面で容易
に分解され酸素となる(O3→O2)。本発明の処理装置
によれば、一つの装置で上記オゾンの発生及び分解をそ
の場の状況に応じて、あるいは自動制御的に制御するこ
とができる。従って、従来の装置では不可能であった目
的に応じたオゾンによる空気の処理を正確かつ簡便に行
うことができまた装置をコンパクトにすることができ
る。On the other hand, unreacted ozone is easily decomposed to oxygen on the surface of the catalyst (O 3 → O 2 ). According to the processing apparatus of the present invention, the generation and decomposition of ozone can be controlled by one apparatus according to the situation at the site or automatically. Therefore, the treatment of air with ozone according to the purpose, which is impossible with the conventional apparatus, can be performed accurately and simply, and the apparatus can be made compact.
【図1】本発明のオゾンによる処理装置のうち、主に殺
菌、脱臭、害虫の駆除を前提にした一実施例を示す構成
説明図である。FIG. 1 is an explanatory diagram showing a configuration of an embodiment of a treatment apparatus using ozone according to the present invention mainly on the premise of sterilization, deodorization, and control of pests.
【図2】オゾンによる処理装置のうち、主に脱臭、浮遊
殺菌、鮮度保持を前提にした一実施例を示す構成説明図
である。FIG. 2 is a configuration explanatory view showing one embodiment of a treatment apparatus using ozone mainly on the premise of deodorization, floating sterilization, and maintaining freshness.
【図3】オゾン処理すべき空間とオゾン処理装置との関
係を示す概略図である。FIG. 3 is a schematic diagram showing a relationship between a space to be subjected to ozone treatment and an ozone treatment device.
【図4】本発明の他の実施例のオゾン処理装置を示す構
成説明図である。FIG. 4 is a configuration explanatory view showing an ozone treatment apparatus according to another embodiment of the present invention.
1,2 開口部 3,11 無機系触媒層 4,12 オゾン発生器 5,14 酸担持吸着剤層 6,15 ファン 7 オゾン処理装置 8 オゾン処理すべき空間 9 オゾンセンサ 10,13 エアーポンプ 1, 2 opening 3, 11 inorganic catalyst layer 4, 12 ozone generator 5, 14 acid-carrying adsorbent layer 6, 15 fan 7 ozone treatment device 8 space to be ozone treated 9 ozone sensor 10, 13 air pump
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平3−47261(JP,A) 特開 平3−143526(JP,A) 特開 平2−193672(JP,A) 特開 昭63−214262(JP,A) 特開 昭63−317155(JP,A) 特開 昭54−119371(JP,A) 特開 昭62−57557(JP,A) 特開 昭63−59961(JP,A) 実開 昭64−32728(JP,U) 実開 昭63−197547(JP,U) (58)調査した分野(Int.Cl.7,DB名) A61L 9/015 B01D 53/38 B01D 53/66 B01D 53/74 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-3-47261 (JP, A) JP-A-3-143526 (JP, A) JP-A-2-193672 (JP, A) JP-A-63-1988 214262 (JP, A) JP-A-63-317155 (JP, A) JP-A-54-119371 (JP, A) JP-A-62-57557 (JP, A) JP-A-63-59961 (JP, A) Japanese Utility Model Application No. 64-32728 (JP, U) Japanese Utility Model Application No. 63-197547 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) A61L 9/015 B01D 53/38 B01D 53/66 B01D 53/74
Claims (6)
つの開口部が備えられ、その気体流路内に送風手段、無
声放電式のオゾン発生器、少なくともオゾンを吸着もし
くは分解しうる無機系触媒層および該オゾン発生器に供
給される気体前処理用の酸担持吸着剤層が配置され、送
風手段は、正・逆両方向に送風するための一もしくは複
数のファンと送風方向選択手段とから構成され、かつオ
ゾン発生器は、送風方向選択手段と連動してオゾンの発
生量を調節するための調節手段を具備することを特徴と
するオゾンによる処理装置。1. An apparatus main body is provided with two openings for forming a gas flow path, a blowing means, a silent discharge type ozone generator, and an inorganic material capable of adsorbing or decomposing at least ozone in the gas flow path. A system catalyst layer and an acid-carrying adsorbent layer for gas pretreatment supplied to the ozone generator are arranged, and the blowing means includes one or more fans for blowing in both forward and reverse directions, and blowing direction selecting means. Wherein the ozone generator is provided with adjusting means for adjusting the amount of ozone generated in conjunction with the blowing direction selecting means.
正(又は逆)方向の送風が選択された際、オゾン発生器
のオゾンの発生量を最大側に設定し、一方送風方向選択
手段によって逆(又は正)方向の送風が選択された際オ
ゾン発生器のオゾン発生量を減少側ないし停止側に設定
するものである請求項1記載の装置。2. The adjusting means sets the amount of ozone generated by the ozone generator to the maximum side when the air blowing in the forward (or reverse) direction is selected by the air blowing direction selecting means, while the air blowing direction selecting means sets the amount of ozone generated in the reverse direction. The apparatus according to claim 1, wherein the ozone generation amount of the ozone generator is set to a decreasing side or a stopping side when air blowing in the (or forward) direction is selected.
向選択手段が該タイマーと連動している請求項1記載の
装置。3. The apparatus according to claim 1, wherein a timer is provided in the apparatus main body, and the blowing direction selecting means is linked to the timer.
る請求項1記載の装置。4. The apparatus of claim 1, wherein the fan comprises one reversible fan.
つがそれぞれ正逆両方向に送風しうるよう設定配置され
ている請求項1記載の装置。5. The apparatus according to claim 1, wherein the fan comprises two fans, each of which is arranged so as to be able to blow air in both forward and reverse directions.
正)方向の送風が選択されかつオゾン発生器のオゾン発
生量が停止側に設定された場合、オゾン発生器の電極に
供給する気体で、該電極内がパージされるように制御さ
れる請求項2記載の装置。6. A gas to be supplied to an electrode of the ozone generator when the blower in the reverse (or forward) direction is selected by the blower direction selecting means and the amount of ozone generated by the ozone generator is set to a stop side. 3. The apparatus according to claim 2, wherein the apparatus is controlled to purge the inside of the electrode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3171428A JP3009251B2 (en) | 1990-09-21 | 1991-07-11 | Ozone treatment equipment |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25294990 | 1990-09-21 | ||
| JP2-252949 | 1990-09-21 | ||
| JP3171428A JP3009251B2 (en) | 1990-09-21 | 1991-07-11 | Ozone treatment equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04357956A JPH04357956A (en) | 1992-12-10 |
| JP3009251B2 true JP3009251B2 (en) | 2000-02-14 |
Family
ID=26494161
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3171428A Expired - Fee Related JP3009251B2 (en) | 1990-09-21 | 1991-07-11 | Ozone treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3009251B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3430540B2 (en) * | 1993-02-26 | 2003-07-28 | いすゞ自動車株式会社 | Ozone deodorization system |
| US20130287626A1 (en) * | 2006-11-21 | 2013-10-31 | Karen Benedek | Apparatus and method for treating impurities in air and materials |
-
1991
- 1991-07-11 JP JP3171428A patent/JP3009251B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04357956A (en) | 1992-12-10 |
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