JP2001276199A - Deodorization adsorption oxidizer and adsorption oxidation process by using it - Google Patents
Deodorization adsorption oxidizer and adsorption oxidation process by using itInfo
- Publication number
- JP2001276199A JP2001276199A JP2000134021A JP2000134021A JP2001276199A JP 2001276199 A JP2001276199 A JP 2001276199A JP 2000134021 A JP2000134021 A JP 2000134021A JP 2000134021 A JP2000134021 A JP 2000134021A JP 2001276199 A JP2001276199 A JP 2001276199A
- Authority
- JP
- Japan
- Prior art keywords
- adsorption
- deodorizing
- oxidizer
- titanium oxide
- oxidizing agent
- 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
Links
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 32
- 239000007800 oxidant agent Substances 0.000 title claims abstract description 21
- 230000003647 oxidation Effects 0.000 title claims abstract description 17
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 17
- 238000000034 method Methods 0.000 title claims abstract description 15
- 238000004332 deodorization Methods 0.000 title abstract description 5
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 35
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 25
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims abstract description 25
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000003546 flue gas Substances 0.000 claims abstract description 7
- 238000002485 combustion reaction Methods 0.000 claims abstract description 4
- 238000001035 drying Methods 0.000 claims abstract 2
- 230000001877 deodorizing effect Effects 0.000 claims description 17
- 239000003795 chemical substances by application Substances 0.000 claims description 14
- 239000003463 adsorbent Substances 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims description 9
- 239000000356 contaminant Substances 0.000 claims description 7
- 239000007921 spray Substances 0.000 claims description 4
- 238000005245 sintering Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 32
- 239000003344 environmental pollutant Substances 0.000 abstract description 4
- 231100000719 pollutant Toxicity 0.000 abstract description 4
- 239000000809 air pollutant Substances 0.000 abstract description 3
- 231100001243 air pollutant Toxicity 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- 239000003517 fume Substances 0.000 abstract 1
- 239000010457 zeolite Substances 0.000 description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 24
- 229910021536 Zeolite Inorganic materials 0.000 description 23
- 239000000843 powder Substances 0.000 description 17
- 230000000694 effects Effects 0.000 description 5
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 239000010419 fine particle Substances 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 230000000274 adsorptive effect Effects 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 3
- 235000011116 calcium hydroxide Nutrition 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 244000144972 livestock Species 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000010936 titanium Substances 0.000 description 3
- 229910052719 titanium Inorganic materials 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 210000003298 dental enamel Anatomy 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000006864 oxidative decomposition reaction Methods 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 238000006303 photolysis reaction Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 102100032566 Carbonic anhydrase-related protein 10 Human genes 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 101100321669 Fagopyrum esculentum FA02 gene Proteins 0.000 description 1
- 101000867836 Homo sapiens Carbonic anhydrase-related protein 10 Proteins 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 150000004045 organic chlorine compounds Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 230000002195 synergetic effect Effects 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
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Catalysts (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、脱臭吸着酸化処理剤と
その処理剤による吸着酸化処理方法に関し、特に、この
脱臭吸着酸化処理剤を焼却設備や燃焼設備の煙道ガスに
散布し、或いは被処理物質に表面散布し、屋外処分場で
太陽光により或いは紫外線照射下でそれら成分を分解処
理することによって有害な大気汚染物質を処理する安価
な吸着酸化処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deodorizing adsorptive oxidizing agent and a method for adsorbing and oxidizing the same by using the treating agent. The present invention relates to an inexpensive adsorptive oxidation treatment method for treating harmful air pollutants by spraying a surface on a substance to be treated and decomposing those components by sunlight or ultraviolet irradiation at an outdoor disposal site.
【0002】[0002]
【従来の技術】大気汚染物質の処理剤には例えば、活性
炭、消石灰、酸化アルミナおよびゼオライトなどがあ
る。活性炭は、それぞれの汚染物質に応じて適応させる
ことができる代表的吸着剤であり、アンモニア、硫化水
素、トリメチルアミンその他有機溶剤などの吸着に絶大
なる信頼性がある。しかし、活性炭自体が可燃性である
ので焼却ガスなどの高温ガスを吸着することはできなか
った。また、高濃度ガス成分を吸着するには活性炭の単
価が高く、運転コストが非常に高くなる欠点があった。
消石灰、酸化アルミナなどは化学的特性から特定のガス
成分にしか適用できない欠点があった。一方、ガス処理
装置関連としての従来の技術には、以下の通りのものが
ある。例えば排気ガスに対して活性炭吸着塔などのよう
に吸着塔設備を採用している。消石灰、酸化アルミナな
ども同様に吸着設備を必要としている。いずれにしても
これらの設備は建設費が高く施工主にはかなりの負担に
なっている。このように悪臭防止や大気汚染防止装置
は、それらの装置の建設費、運転管理費、維持管理費は
莫大であるとともに維持管理面で大変複雑なものであ
り、それらの施設が生産性施設ではなく、非生産性施設
であることから、それらの設置者にとってはことさら大
変な負担である。2. Description of the Related Art Activated carbon, slaked lime, alumina oxide and zeolite are examples of agents for treating air pollutants. Activated carbon is a representative adsorbent that can be tailored to each pollutant and has tremendous reliability in adsorbing ammonia, hydrogen sulfide, trimethylamine and other organic solvents. However, since activated carbon itself is flammable, high-temperature gas such as incineration gas cannot be adsorbed. In addition, the cost of activated carbon is high for adsorbing high-concentration gas components, and the operating cost is extremely high.
Slaked lime, alumina oxide and the like have a drawback that they can be applied only to specific gas components due to their chemical properties. On the other hand, there are the following related arts related to the gas processing apparatus. For example, adsorption tower equipment such as an activated carbon adsorption tower is used for exhaust gas. Slaked lime, alumina oxide and the like also require adsorption equipment. In any case, these equipments are expensive to construct and put a considerable burden on the contractor. As described above, the odor control and air pollution control devices require huge construction costs, operation management costs, and maintenance costs, and are extremely complicated in terms of maintenance. And it is a non-productive facility, which puts a heavy burden on those installers.
【0003】[0003]
【発明が解決しようとする課題】本発明者は、上述のよ
うな欠点を解決すべく、単純な処理剤と簡単な処理方法
や処理装置により処理することができないか鋭意研究を
重ねてきた。その結果、従来の活性炭などの吸着剤は汚
染物質の大半を吸着する反面すぐに飽和吸着量に達し、
そのために活性炭の交換や使用済み活性炭の再生のため
に高い費用がかかるために前処理技術を採用せざるを得
なかった。また、それら吸着塔を含むガス吸着処理設備
は設備費が高額で、運転管理も複雑であり、維持管理費
もかさみ、その上広大な敷地が要求されるため普及しに
くいことが分かった。本発明者は、酸化チタン微粒子が
活性炭と同様の吸着性能を有し、かつ紫外線との併用で
殺菌処理や有機物の分解をより促進できるといった知見
を予め得ていたのであるが、酸化チタン微粒子のままで
は処理後のガスとの分離など取扱が困難であるため、実
用化されるには至らなかった。そこで本発明者は、ゼオ
ライトをある一定温度範囲で電気加熱乾燥すれば、表面
が多孔質で、その多孔質の表面積がマクロ・ミクロにわ
たり活性炭と同等な特性をもつ担体となり、その担体に
酸化チタンを担持固定化した担持体が酸化チタン微粒子
の特性と吸着剤の特性の両方を保持できることに着目
し、それを吸着酸化処理剤としての利用を試みた。この
吸着酸化処理剤は有機成分をより速く吸着することがで
きるとともに、太陽光線照射または紫外線照射またはオ
ゾンランプ照射との併用により吸着した有機成分をより
速く酸化分解することを見出た。そこで本発明は、ゼオ
ライトの中でも直経1mm以下のもので取り扱いにくく
商品価値のない微小ゼオライトに主眼をおき、その微小
ゼオライトに酸化チタンを担持した吸着促進剤などを用
いてガス成分を吸着処理させ、それに太陽光線中の紫外
線を屋外などで照射させ、或いは紫外線ランプ又はオゾ
ンランプの照射により自然光又は人工光による化学酸化
分解処理させることを課題とする。In order to solve the above-mentioned drawbacks, the present inventor has intensively studied whether or not the treatment can be performed with a simple treating agent and a simple treating method or treating apparatus. As a result, conventional adsorbents such as activated carbon adsorb most of the pollutants, but quickly reach the saturated adsorption amount,
Therefore, high cost is required for replacement of activated carbon and regeneration of used activated carbon, so that pretreatment technology has to be adopted. In addition, it has been found that the gas adsorption treatment equipment including these adsorption towers has high equipment costs, complicated operation and management, high maintenance and management costs, and furthermore, a large site is required, so that it is difficult to spread the equipment. The present inventor had previously obtained the knowledge that titanium oxide fine particles have the same adsorption performance as activated carbon, and can further promote the sterilization treatment and decomposition of organic substances in combination with ultraviolet rays. As it is difficult to handle such as separation from the gas after treatment as it is, it has not been put to practical use. The inventor of the present invention has proposed that if zeolite is electrically heated and dried in a certain temperature range, the surface becomes porous, and the surface area of the porous material becomes a carrier having characteristics equivalent to that of activated carbon over a macro-micro area. Paying attention to the fact that the carrier having immobilized thereon can retain both the properties of titanium oxide fine particles and the properties of the adsorbent, we attempted to use it as an adsorbent oxidation treatment agent. It has been found that this adsorbing and oxidizing agent is capable of adsorbing organic components more quickly, and oxidatively decomposes the adsorbed organic components more quickly when used in combination with irradiation with sunlight, ultraviolet rays or ozone lamps. Therefore, the present invention focuses on small zeolites having a diameter of 1 mm or less, which are difficult to handle and have no commercial value, among zeolites. It is another object of the present invention to irradiate ultraviolet rays in sunlight outdoors or the like, or to perform chemical oxidative decomposition treatment by natural light or artificial light by irradiation with an ultraviolet lamp or an ozone lamp.
【0004】[0004]
【課題を解決するための手段】本発明は酸化チタン液を
直経1mm以下のゼオライト粒子に重量比で2〜10%
になるように表面に塗布し、常温で乾燥させ固定化させ
た脱臭吸着酸化処理剤である。本発明はまた、酸化チタ
ン液を直経1mm以下のゼオライト粒子に重量比で2〜
10%になるように表面に塗布し、それを温度200〜
400℃で燒結処理した脱臭吸着酸化処理剤である。本
発明はまた、酸化チタン液を直経1mm以下のゼオライ
ト粒子に重量比で2〜10%になるように表面に塗布
し、常温で乾燥させ固定化させた脱臭吸着酸化処理剤を
焼却設備や燃焼設備の煙道ガスに散布し、臭気成分や汚
染成分を吸着させ、バグフィルターでその乾燥脱臭吸着
酸化処理剤を回収し、屋外処分場で太陽光により或いは
紫外線照射下でそれら成分を分解処理する脱臭吸着酸化
処理剤による吸着酸化処理方法である。本発明はまた、
酸化チタン液を直経1mm以下のゼオライト粒子に重量
比で2〜10%になるように表面に塗布し、それを温度
200〜400℃で燒結処理した脱臭吸着酸化処理剤
を、臭気成分或いは汚染成分を有する被処理物質に表面
散布し、臭気成分或いは汚染成分を吸着させるととも
に、屋外処分場で太陽光により或いは紫外線照射下でそ
れら成分を分解処理する脱臭吸着酸化処理剤による吸着
酸化処理方法である。According to the present invention, a titanium oxide solution is added to zeolite particles having a diameter of 1 mm or less in a weight ratio of 2 to 10%.
This is a deodorizing, adsorption and oxidizing agent that is applied to the surface so as to be dried, fixed at room temperature and fixed. The present invention also relates to a method in which titanium oxide liquid is added to zeolite particles having a diameter of 1 mm or less in a weight ratio of 2 to 2.
It is applied to the surface so as to be 10%, and the temperature is 200-
It is a deodorizing adsorption oxidizing agent sintered at 400 ° C. The present invention also provides a deodorizing adsorption oxidizing agent which is applied to a surface of a zeolite particle having a diameter of 1 mm or less in a weight ratio of 2 to 10% and dried and fixed at room temperature. Spray to the flue gas of the combustion equipment to adsorb odorous and contaminant components, collect the dry deodorized adsorbent oxidizing agent with a bag filter, and decompose these components by sunlight or ultraviolet irradiation at an outdoor disposal site This is an adsorption oxidation treatment method using a deodorizing adsorption oxidation treatment agent. The present invention also provides
A titanium oxide solution is applied to the surface of zeolite particles having a diameter of 1 mm or less in a weight ratio of 2 to 10%, and is sintered at a temperature of 200 to 400 ° C. The surface is scattered on the material to be treated having the components, and the odor component or the contaminant component is adsorbed. At the outdoor disposal site, the component is decomposed by sunlight or ultraviolet irradiation. is there.
【0005】[0005]
【作用】本発明は、ゼオライトの中でも直経1mm以下
のゼオライト粒子のように小さくて取り扱いにくく、微
少すぎて商品価値がないようなゼオライトに主眼をおき
その微小ゼオライトに酸化チタンを担持した吸着促進剤
などを用いてガス成分を吸着処理させ、それに太陽光線
中の紫外線を屋外などで照射させ、或いは紫外線ランプ
又はオゾンランプの照射により自然光又は人工光による
化学酸化分解処理させるものである。本発明者は、兼ね
てより光触媒作用によって悪臭成分を分解し無臭化する
ことを研究してきたが、それは粉末酸化チタンなどの光
触媒と専用紫外線ランプ(主に370nm波長)を使用
した実験室規模のものであった。本発明者は、表面が多
孔質で且つその多孔質の表面積がマクロ・ミクロにわた
り大きなゼオライト微粒子を担体とし、その担体に酸化
チタンを担持固定化した担持体が酸化チタン微粒子の特
性とモレキュラーシーブス(合成ゼオライト)のの特性
の両方を保持できることに着目し、それを吸着酸化処理
剤として用いることでその処理剤に吸着した有機物を分
解するために、煙道ガス処理や最終処分場などの一般廃
棄物、焼却灰等への散布処理による消臭、排ガス成分分
解について実用化の可能性があるのではと思いたち、各
種試験を試みた結果その処理性能のいろいろな点で優位
性を見いだした。 1)本発明は、酸化チタン液を直経1mm以下のゼオラ
イト粒子に重量比で2〜10%になるように表面に塗布
し、常温で乾燥させ固定化させた脱臭吸着酸化処理剤で
ある。この常温乾燥固定化脱臭吸着酸化処理剤は、酸化
チタンの微粉末とゼオライト粉末のそれぞれの特性が損
なわれることなく相乗効果を得ることができる。即ち微
粉末であることの特長を活かす処理方法に利用すること
により、長所を発揮できることになる。またゼオライト
特有の陽イオン交換能や高温下でゼオライトの付着水や
結晶水が蒸発した際にできる多孔質により、さらにそれ
に伴ってアルミや鉄成分が酸化アルミや酸化鉄に変化し
て排ガス成分の吸着性能を活性炭と同等以上に発揮する
ことができる。 2)上記の長所を活かした排ガス処理方法として、吸着
塔設備を必要とすることなく、高温の煙道ガスにその吸
着酸化処理剤を噴霧することにより煙道ガスの汚染成分
を効率よく吸着し、その後にバグフィルターなどで吸着
済み微粉末を容易に回収することができる。また、その
集塵スラッジを大気に拡散することなく屋外処分場など
で太陽光照射下で酸化チタンの光分解性能で吸着成分を
分解することができる。 3)本発明は、酸化チタン液をゼオライト粉末に予め温
度200〜400℃で燒結処理して、ゼオライトの付着
水や結晶水が蒸発した際にできる多孔質により、さらに
それに伴ってアルミや鉄成分が酸化アルミや酸化鉄に変
化して排ガス成分の吸着性能を活性炭と同等以上に発揮
することができる。 4)上記吸着酸化処理剤を屋外処分場などの一般廃棄物
や焼却灰等などに被膜するように散布することによっ
て、排ガス成分や有害成分を大気に放散することなく、
太陽光照射下で酸化チタンの光分解性能で吸着成分を分
解することができる。The present invention focuses on zeolite particles which are small and difficult to handle, such as zeolite particles having a diameter of 1 mm or less, and which are too small to have commercial value among zeolite. A gas component is adsorbed using an agent or the like, and ultraviolet rays in sunlight are irradiated outdoors or the like, or a chemical oxidative decomposition treatment is performed by natural light or artificial light by irradiation with an ultraviolet lamp or an ozone lamp. The present inventor has been studying to decompose and deodorize malodorous components by photocatalysis, but it is a laboratory scale using a photocatalyst such as powdered titanium oxide and a dedicated ultraviolet lamp (mainly 370 nm wavelength). Was something. The inventor of the present invention has reported that a carrier in which a zeolite fine particle having a porous surface and a large porous surface area over a macro-micro area is used as a carrier, and the titanium oxide is immobilized on the carrier, and the characteristics of the titanium oxide fine particle and the molecular sieves ( Focusing on the ability to maintain both the properties of synthetic zeolites) and using it as an adsorbent oxidizing agent, it decomposes organic substances adsorbed by the treating agent. We thought that there is a possibility of practical application of deodorization and exhaust gas component decomposition by spraying on materials and incineration ash, etc., and as a result of various tests, we found superiority in various points of treatment performance. 1) The present invention is a deodorizing adsorption oxidation treatment agent in which a titanium oxide liquid is applied to zeolite particles having a diameter of 1 mm or less in a weight ratio of 2 to 10% and dried and fixed at room temperature. This deodorizing adsorption oxidation treatment agent fixed at room temperature can obtain a synergistic effect without impairing the respective properties of the fine powder of titanium oxide and the zeolite powder. In other words, the advantages can be exhibited by utilizing the treatment method utilizing the characteristics of the fine powder. In addition, due to the cation exchange capacity peculiar to zeolite and the porosity formed when the water adhering to the zeolite and the water of crystallization evaporate at high temperatures, the aluminum and iron components change to aluminum oxide and iron oxide as a result. Adsorption performance can be exhibited at least as high as that of activated carbon. 2) As an exhaust gas treatment method that takes advantage of the above advantages, by spraying the adsorption oxidation treatment agent onto a high-temperature flue gas without adsorbing tower equipment, the flue gas contaminants can be efficiently adsorbed. Then, the adsorbed fine powder can be easily collected by a bag filter or the like. In addition, the adsorbed component can be decomposed by the photodecomposition performance of titanium oxide under sunlight irradiation in an outdoor disposal site or the like without diffusing the dust collection sludge into the atmosphere. 3) According to the present invention, a titanium oxide solution is sintered to a zeolite powder in advance at a temperature of 200 to 400 ° C., and a porous material formed when water adhering to the zeolite or water of crystallization evaporates. Can be changed to aluminum oxide or iron oxide to exhibit the adsorption performance of exhaust gas components at least as high as that of activated carbon. 4) By spraying the adsorbed oxidizing agent so as to cover general waste such as an outdoor disposal site or incinerated ash, etc., without discharging exhaust gas components and harmful components to the atmosphere.
Adsorbed components can be decomposed by the photodecomposition performance of titanium oxide under sunlight irradiation.
【0006】[0006]
【実施例1】常温乾燥酸化チタン担持ゼオライト粉末は
以下の工程で製造する。 1)ゼオライト粉末1リツトルを琺瑯パットに平滑に置
く。 2)25%の酸化チタンを固形分としたゾル(昭和電工
製ジュピター)100mlをゼオライト粉末を掻き混ぜ
ながら噴霧する。 3)天日にてそれぞれのゼオライト粉末が互いに付着す
ることのない状態で乾燥する。Example 1 A room temperature dried titanium oxide-supported zeolite powder is produced by the following steps. 1) 1 liter of zeolite powder is placed evenly on an enamel pad. 2) Spray 100 ml of a sol (Jupiter manufactured by Showa Denko) containing 25% titanium oxide as a solid content while stirring the zeolite powder. 3) Dry each zeolite powder on the sun without adhering to each other.
【0007】[0007]
【実施例2】実施例1で製造した酸化チタン担持のゼオ
ライト粉末を、図1に示すように、焼却炉1に接続する
煙道ガス排出管2内の排出煙道に酸化チタン担持粉末ゼ
オライト供給装置5から散布し、排ガス汚染成分を吸着
した酸化チタン担持のゼオライト粉末と処理ガスから粉
塵を同時にバグフィルター3で集塵する。排ガス汚染成
分が除去された処理ガスはガス排出管4から放出され
る。バグフィルター3で集塵された焼却灰は集塵灰排出
管6から排出され、焼却灰処分場7へ送られ、その屋外
で太陽光線にあたるようにして酸化チタンと太陽光の紫
外線で吸着排ガス汚染物質を光分解させる。この実施例
2のガス処理装置を用いて、畜産堆肥化設備の排気ガス
に対して以下の処理条件にて処理を行った。 本発明の処理結果により塩基性、酸性いずれかのガスに
対しても高い処理効果認められる。また、焼却灰臭気も
より安定して処理効果が得られている。EXAMPLE 2 The zeolite powder supporting titanium oxide produced in Example 1 was supplied to the exhaust flue in a flue gas discharge pipe 2 connected to an incinerator 1 as shown in FIG. The dust is simultaneously collected by the bag filter 3 from the treatment gas and the titanium oxide-supported zeolite powder which is sprayed from the device 5 and adsorbs the exhaust gas contaminant. The processing gas from which the exhaust gas pollutant has been removed is discharged from the gas discharge pipe 4. The incinerated ash collected by the bag filter 3 is discharged from the collected ash discharge pipe 6 and sent to the incineration ash disposal site 7, where it is exposed to sunlight and the exhaust gas is contaminated with titanium oxide and ultraviolet rays of sunlight. Photodegrade the substance. Using the gas processing apparatus of Example 2, the exhaust gas of the livestock composting facility was processed under the following processing conditions. According to the processing results of the present invention, a high processing effect is recognized even for either a basic or acidic gas. In addition, the incineration ash odor is more stably obtained.
【0008】[0008]
【実施例3】電気加温による酸化チタン担持ゼオライト
粉末は以下の工程で製造する。 1)ゼオライト粉末1リツトルを琺瑯パットに平滑に置
く。 2)25%の酸化チタンを固形分としたゾル(昭和電工
製ジュピター)100mlをゼオライト粉末を掻き混ぜ
ながら噴霧する。 3)電気炉又はマイクロ照射加熱により、2)項の酸化
チタン撒布の粉末ゼオライトを温度200〜400゜C
で燒結処理した。Example 3 A zeolite powder supporting titanium oxide by electric heating is produced by the following steps. 1) 1 liter of zeolite powder is placed evenly on an enamel pad. 2) Spray 100 ml of a sol (Jupiter manufactured by Showa Denko) containing 25% titanium oxide as a solid content while stirring the zeolite powder. 3) By heating in an electric furnace or micro irradiation, the powdered zeolite sprayed with titanium oxide of the item 2) is heated to a temperature of 200 to 400 ° C.
For sintering.
【0009】[0009]
【実施例4】図2の装置において、酸化チタン担持のゼ
オライト粉末を供給しなかった場合の焼却灰の表面に、
実施例1で製造した酸化チタン担持のゼオライト粉末を
2cmの厚さになるように被覆した。その結果その表
面から発散している臭気濃度は以下の通りである。 本発明の処理装置により塩基性、酸性いずれかのガスに
対しても高い処理効果が認められる。Embodiment 4 In the apparatus of FIG. 2, the surface of the incinerated ash when the zeolite powder supporting titanium oxide was not supplied,
The titanium oxide-supported zeolite powder produced in Example 1 was coated to a thickness of 2 cm. As a result, the odor concentration emanating from the surface is as follows. The processing apparatus of the present invention shows a high processing effect on either basic or acidic gas.
【0010】[0010]
【効果】本発明の脱臭吸着酸化処理剤を用いた排ガス処
理方法は、畜産関係の畜舎や堆肥化場、下水処理場前処
理設備、糞尿処理場前処理設備、農村集落排水設備など
の臭気発生箇所のガス処理設備に有効なものである。特
に、有機塩素系排ガスなどが発生するごみ焼却設備や産
業廃棄物処分場、一般廃棄物処分場などで高濃度で発生
する臭気発生箇所に対して、本発明による脱臭吸着酸化
処理剤およびそれを用いた排ガス処理方法を用いれば、
排ガス処理装置に新たに吸着設備の増設も必要でなく、
また、処分場で被処理物質を被覆した吸着剤は光再生さ
れるので新たに追加したり交換したり、吸着剤を新たに
再生させる必要がないことから環境に悪影響を及ぼすこ
とがなく、大幅な運転経費の削減になるなどの効果があ
る。また、本発明は有機系成分、特に、有機塩素化合
物、窒素酸化物などの工場からの有害ガスの処理にも優
れた効果があり、環境浄化設備や公害防止設備として有
効であり、運転経費や建設費削減の上からきわめて効果
的である。[Effect] The exhaust gas treatment method using the deodorizing adsorptive oxidation treatment agent of the present invention is applicable to livestock-related livestock pens, composting plants, sewage treatment plant pretreatment facilities, manure treatment plant pretreatment facilities, rural village drainage facilities, etc. This is effective for gas treatment facilities at locations. In particular, the deodorizing adsorption oxidation treatment agent according to the present invention and the deodorizing adsorption oxidizing agent according to the present invention are applied to odor generating places generated at high concentration in garbage incinerators, industrial waste disposal sites, general waste disposal sites, etc. where organic chlorine-based exhaust gas and the like are generated. If the used exhaust gas treatment method is used,
It is not necessary to add new adsorption equipment to the exhaust gas treatment device.
In addition, since the adsorbent coated with the substance to be treated at the disposal site is regenerated by light, there is no need to add or replace it, and there is no need to regenerate the adsorbent. This has the effect of greatly reducing operating costs. In addition, the present invention has an excellent effect on treating harmful gases from factories such as organic components, in particular, organochlorine compounds and nitrogen oxides, and is effective as an environmental purification facility or a pollution prevention facility. This is extremely effective in reducing construction costs.
【図1】本発明の脱臭吸着酸化処理剤による吸着酸化処
理方法をゴミ焼却炉に実施した場合の排ガスの処理フロ
ーを示した概念図である。FIG. 1 is a conceptual diagram showing a processing flow of exhaust gas when an adsorption oxidation treatment method using a deodorizing adsorption oxidation treatment agent of the present invention is applied to a garbage incinerator.
1 焼却炉 2
煙道ガス排出管 3 バグフィルター 4
ガス排出管 5 酸化チタン担持粉末ゼオライト供給装置 6 集塵灰排出管 7
焼却灰処分場1 incinerator 2
Flue gas exhaust pipe 3 Bag filter 4
Gas discharge pipe 5 Titanium oxide supported powder zeolite supply device 6 Dust collection ash discharge pipe 7
Incineration ash disposal site
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 53/86 ZAB B01J 35/02 J B01J 29/06 20/18 E 35/02 B01D 53/36 J // B01J 20/18 ZABH Fターム(参考) 4C080 AA05 AA07 BB02 CC03 CC04 CC05 CC08 CC09 HH05 JJ04 KK06 KK08 LL02 MM02 MM04 QQ03 4D048 AA22 AB01 AB03 BA07X BA11X BA41X BB01 CB04 CC39 CD01 CD05 EA01 EA04 4G066 AA61B BA09 BA20 CA02 DA02 FA14 FA22 FA34 FA37 4G069 AA03 AA08 BA04A BA04B BA07A BA07B BA48A CA02 CA04 CA07 CA10 CA17 DA08 EA01X EA01Y EB18X FA02 FB23 FB33 FC07 FC08 ZA01A ZA01B ZA46A ZA46B ZE09──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) B01D 53/86 ZAB B01J 35/02 J B01J 29/06 20/18 E 35/02 B01D 53/36 J / / B01J 20/18 ZABH F-term (Reference) 4C080 AA05 AA07 BB02 CC03 CC04 CC05 CC08 CC09 HH05 JJ04 KK06 KK08 LL02 MM02 MM04 QQ03 4D048 AA22 AB01 AB03 BA07X BA11X BA41X BB01 CB04 BA01 FA04 FA34 FA37 4G069 AA03 AA08 BA04A BA04B BA07A BA07B BA48A CA02 CA04 CA07 CA10 CA17 DA08 EA01X EA01Y EB18X FA02 FB23 FB33 FC07 FC08 ZA01A ZA01B ZA46A ZA46B ZE09
Claims (4)
ト粒子に重量比で2〜10%になるように表面に塗布
し、常温で乾燥させ固定化させた脱臭吸着酸化処理剤。1. A deodorizing and adsorbing oxidizing agent obtained by applying a titanium oxide solution to zeolite particles having a diameter of 1 mm or less in a weight ratio of 2 to 10% and drying and fixing at room temperature.
ト粒子に重量比で2〜10%になるように表面に塗布
し、それを温度200〜400℃で燒結処理した脱臭吸
着酸化処理剤。2. A deodorizing and adsorbing oxidizing agent obtained by applying a titanium oxide solution to zeolite particles having a diameter of 1 mm or less on the surface so as to have a weight ratio of 2 to 10% and subjecting it to a sintering treatment at a temperature of 200 to 400 ° C.
ト粒子に重量比で2〜10%になるように表面に塗布
し、常温で乾燥させ固定化させた脱臭吸着酸化処理剤を
焼却設備や燃焼設備の煙道ガスに散布し、臭気成分や汚
染成分を吸着させ、バグフィルターでその乾燥脱臭吸着
酸化処理剤を回収し、屋外処分場で太陽光により或いは
紫外線照射下でそれら成分を分解処理する脱臭吸着酸化
処理剤による吸着酸化処理方法。3. A deodorizing and adsorbing oxidizing agent which has been applied to a surface of zeolite particles having a diameter of 1 mm or less in a weight ratio of 2 to 10% and dried and fixed at room temperature. Spray to the flue gas of the combustion equipment to adsorb odorous and contaminant components, collect the dry deodorized adsorbent oxidizing agent with a bag filter, and decompose these components by sunlight or ultraviolet irradiation at an outdoor disposal site Oxidation treatment method using a deodorizing adsorption oxidation treatment agent.
ト粒子に重量比で2〜10%になるように表面に塗布
し、それを温度200〜400℃で燒結処理した脱臭吸
着酸化処理剤を、臭気成分或いは汚染成分を有する被処
理物質に表面散布し、臭気成分或いは汚染成分を吸着さ
せるとともに、屋外処分場で太陽光により或いは紫外線
照射下でそれら成分を分解処理する脱臭吸着酸化処理剤
による吸着酸化処理方法。4. A deodorizing and adsorbing oxidizing agent obtained by applying a titanium oxide solution to zeolite particles having a diameter of 1 mm or less in a weight ratio of 2 to 10% and sintering it at a temperature of 200 to 400 ° C. A deodorizing and adsorbing oxidizing agent that spreads on the surface of a substance having an odor component or a contaminant component to adsorb the odor component or the contaminant component and decomposes the component by sunlight or ultraviolet irradiation at an outdoor disposal site. Adsorption oxidation treatment method.
Priority Applications (1)
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---|---|---|---|
JP2000134021A JP2001276199A (en) | 2000-03-30 | 2000-03-30 | Deodorization adsorption oxidizer and adsorption oxidation process by using it |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000134021A JP2001276199A (en) | 2000-03-30 | 2000-03-30 | Deodorization adsorption oxidizer and adsorption oxidation process by using it |
Publications (1)
Publication Number | Publication Date |
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JP2001276199A true JP2001276199A (en) | 2001-10-09 |
Family
ID=18642375
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JP (1) | JP2001276199A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006077367A (en) * | 2004-09-10 | 2006-03-23 | Kyodo Printing Co Ltd | Deodorant coating and deodorant decorative paper |
KR101682907B1 (en) * | 2016-07-22 | 2016-12-19 | 재단법인 철원플라즈마 산업기술연구원 | Adsorbent media, the preparation method thereof, circulation adsorption column for removing the nitrogen and phosphorus compounds |
CN111437723A (en) * | 2020-05-15 | 2020-07-24 | 四川轻化工大学 | Blocking and adsorbing integrated device for VOC gas |
-
2000
- 2000-03-30 JP JP2000134021A patent/JP2001276199A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006077367A (en) * | 2004-09-10 | 2006-03-23 | Kyodo Printing Co Ltd | Deodorant coating and deodorant decorative paper |
KR101682907B1 (en) * | 2016-07-22 | 2016-12-19 | 재단법인 철원플라즈마 산업기술연구원 | Adsorbent media, the preparation method thereof, circulation adsorption column for removing the nitrogen and phosphorus compounds |
CN111437723A (en) * | 2020-05-15 | 2020-07-24 | 四川轻化工大学 | Blocking and adsorbing integrated device for VOC gas |
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