JPH02139017A - Deodorizing process - Google Patents
Deodorizing processInfo
- Publication number
- JPH02139017A JPH02139017A JP63293929A JP29392988A JPH02139017A JP H02139017 A JPH02139017 A JP H02139017A JP 63293929 A JP63293929 A JP 63293929A JP 29392988 A JP29392988 A JP 29392988A JP H02139017 A JPH02139017 A JP H02139017A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- catalyst
- smelly
- adsorption
- carbon layer
- 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
- 238000000034 method Methods 0.000 title claims abstract description 11
- 230000001877 deodorizing effect Effects 0.000 title claims description 21
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 32
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000003054 catalyst Substances 0.000 claims abstract description 24
- 238000001179 sorption measurement Methods 0.000 abstract description 7
- 238000012423 maintenance Methods 0.000 abstract description 2
- 230000008929 regeneration Effects 0.000 abstract description 2
- 238000011069 regeneration method Methods 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract 4
- 239000007789 gas Substances 0.000 description 8
- 239000002253 acid Substances 0.000 description 7
- 235000019645 odor Nutrition 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 230000004931 aggregating effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 230000008786 sensory perception of smell Effects 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明はオゾンを利用する脱臭方法に関し、詳細には悪
臭成分をほぼ完全に除去でき且つ長期間に亘って脱臭性
能を維持できる脱臭方法に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a deodorizing method using ozone, and more particularly to a deodorizing method that can almost completely remove malodorous components and maintain deodorizing performance for a long period of time. It is something.
[従来の技術〕
冷蔵庫等の食品貯蔵庫或はトイレや家畜台等から発生す
る悪臭、さらには各f!産業排気ガス中の悪臭を脱臭す
る手段としてオゾンを利用する方法がある。第3図は上
記脱臭に用いられる脱臭装置、1の概略説明図である。[Prior Art] Bad odors emitted from food storage areas such as refrigerators, toilets, livestock stands, etc., and even f! There is a method of using ozone as a means to deodorize bad odors in industrial exhaust gas. FIG. 3 is a schematic explanatory diagram of a deodorizing device 1 used for the above deodorizing.
該脱臭装置1内には吸気口2と排気口3の間を連通ずる
通気路4が形成され、吸気口3側から排気口側へ向かっ
て順にオゾン発生器5.オゾン・悪臭成分混合室6.触
媒層7及び吸気ファン8が設けられる。該オゾン発生器
5は、高電圧を発生するトランス10と接続されている
。A ventilation path 4 is formed in the deodorizing device 1 and communicates between an intake port 2 and an exhaust port 3, and an ozone generator 5. Ozone/malodorous component mixing chamber 6. A catalyst layer 7 and an intake fan 8 are provided. The ozone generator 5 is connected to a transformer 10 that generates high voltage.
従ってアンモニア、硫化水素等の悪臭ガスを含んだ空気
は吸気ファン8の吸引力によって脱臭装置1の通気路4
内へ矢印六方向に吸い込まれ、オゾン発生器5において
発生されるオゾンと混合室6内で混合され、次いで触媒
層フヘ矢印C方向に沿って送給される。そして該触媒層
7において悪臭ガスは酸化されて無臭成分まで分解処理
され、排気口3から機外へ放出される(矢印D)。Therefore, the air containing malodorous gases such as ammonia and hydrogen sulfide is removed from the air passage 4 of the deodorizing device 1 by the suction force of the intake fan 8.
The ozone is sucked into the interior in the direction of the arrow C, mixed with ozone generated in the ozone generator 5 in the mixing chamber 6, and then fed to the catalyst layer along the direction of the arrow C. In the catalyst layer 7, the malodorous gas is oxidized and decomposed into odorless components, which are then discharged outside the machine from the exhaust port 3 (arrow D).
[発明が解決しようとする課題]
オゾン分解処理においては、酢酸やプロピオン酸等の酸
成分はやや分解しにくく、一部分解せずにそのまま排気
口3より排出されることがある。[Problems to be Solved by the Invention] In ozone decomposition treatment, acid components such as acetic acid and propionic acid are somewhat difficult to decompose, and may be discharged as they are from the exhaust port 3 without being partially decomposed.
また悪臭ガス中にアルコールやアルデヒドが含まれてい
る場合、オゾン分解処理によって対応する酸にまで酸化
されるものの、その後一部分解しきれない酸が排気口3
より排出されることがある。In addition, if alcohol or aldehyde is included in the foul-smelling gas, it will be oxidized to the corresponding acid by ozone decomposition treatment, but the acid that cannot be partially decomposed will be left at the exhaust port 3.
may be excreted.
そのため処理後のガスに該酸成分による臭気が感じられ
、脱臭装置に対する信頼性を低下させることがあった。Therefore, the odor caused by the acid component is felt in the gas after treatment, which may reduce the reliability of the deodorizing device.
そこで本発明者らはオゾン分解処理においても分解され
にくい酸成分の臭いを除去でき、しかも長期にわたって
この脱臭性能を持続することのできる脱臭方法を提供す
る目的で研究を重ね、本発明を完成した。Therefore, the present inventors have conducted extensive research to provide a deodorizing method that can remove the odor of acid components that are difficult to decompose even in ozone decomposition treatment, and can maintain this deodorizing performance over a long period of time, and have completed the present invention. .
[課題を解決するための手段]
上記目的を達成ル得た本発明方法は、悪臭ガスをオゾン
と混合し、触媒の存在下に分解処理した後、未分解臭気
成分を前記触媒の下流側に設けた活性炭層によって吸着
除去することを要旨とするものである。[Means for Solving the Problems] The method of the present invention that achieves the above object mixes malodorous gas with ozone, decomposes it in the presence of a catalyst, and then transports undecomposed malodorous components downstream of the catalyst. The gist of this is to adsorb and remove it using the activated carbon layer provided.
[作用及び実施例]
第1図は本発明方法を通用した脱臭装置の断面説明図で
あり、オゾン発生器5.触媒層7及び吸気ファン8は第
2図に示した従来装置例と同じ順序で通気路4内に構成
される。そして吸気ファン8の下流側には排気口3の手
前位置に活性炭層12が設けられる。従って吸気口2か
ら取り入れられた悪臭ガスを含む空気は、オゾン発生器
5から送り出されるオゾンと混合され、触媒層7を通過
しつつアンモニアや硫化水素等の悪臭成分はここで分解
される。そして該触媒N7において分解されなかった酸
成分等を含む空気はさらに吸気ファン8の吸引力によっ
て活性炭層12へ送給され、ここで空気中に残っている
酸成分等を吸着除去する。この結果排気口3においては
排出空気中に臭気成分を残こすことがない。[Operations and Examples] FIG. 1 is a cross-sectional explanatory diagram of a deodorizing device using the method of the present invention, in which an ozone generator 5. The catalyst layer 7 and the intake fan 8 are arranged in the ventilation passage 4 in the same order as in the conventional device example shown in FIG. An activated carbon layer 12 is provided downstream of the intake fan 8 and in front of the exhaust port 3. Therefore, the air containing malodorous gas taken in from the intake port 2 is mixed with ozone sent out from the ozone generator 5, and while passing through the catalyst layer 7, malodorous components such as ammonia and hydrogen sulfide are decomposed there. The air containing acid components, etc., which has not been decomposed by the catalyst N7 is further fed to the activated carbon layer 12 by the suction force of the intake fan 8, where the acid components, etc. remaining in the air are adsorbed and removed. As a result, no odor components remain in the discharged air at the exhaust port 3.
尚上記の触媒層7は金属もしくは金属酸化物を担体に担
持させたものを使用し格子形状やハニカム形状等のセル
を集合して形成したものを用いるのが一般的であるが特
に限定されない。また活性炭層12は上記触媒層7と同
様ハニカム形状等に成形したり、或は粒状の活性炭を所
定の通気抵抗を発揮する様に充填しても良い、また該活
性炭層12は第1図に示した配設位置に限られず、触媒
層7の下流側であれば吸気ファン8の上流側位置(12
′で示す)であっても良い。The catalyst layer 7 is generally made of a metal or metal oxide supported on a carrier and is formed by aggregating cells in a lattice shape or a honeycomb shape, but is not particularly limited. In addition, the activated carbon layer 12 may be formed into a honeycomb shape or the like similar to the catalyst layer 7, or may be filled with granular activated carbon so as to exhibit a predetermined ventilation resistance. The arrangement position is not limited to the one shown, and if it is downstream of the catalyst layer 7, the upstream position of the intake fan 8 (12
) may also be used.
上記の構成であれば、前記活性炭層12にはオゾン分解
処理後の比較的清浄な空気が送給されるので、該活性炭
層12の吸着性能は吸着飽和まで長期間維持し続けるこ
とができる。また上記触媒層7及び活性炭層12は通気
路4において着脱できる様な構造とし、新品との交換を
容易に行なえる様にしておくことが好ましい。With the above configuration, since relatively clean air after ozone decomposition treatment is supplied to the activated carbon layer 12, the adsorption performance of the activated carbon layer 12 can be maintained for a long period of time until adsorption saturation. Further, it is preferable that the catalyst layer 7 and the activated carbon layer 12 be structured so that they can be attached and detached in the ventilation passage 4, so that they can be easily replaced with new ones.
く実験例〉
第1図に示した構造の脱臭装置を洋式トイレの便座21
側部に取り付け(第2図参照)、使用開始より6力月後
にその脱臭効果を被験者の嗅覚によって判定した。尚触
媒層7には、幾何学表面積が1800m’/a’ 、比
表面積が120 m’/g、セル数が210セル/1n
ch2のハニカム形状の触媒を使用し、また活性炭層1
2はセル数が200セル/1nch2のハニカム形状に
形成した。Experimental example> A deodorizing device with the structure shown in Figure 1 was installed on the toilet seat 21 of a Western-style toilet.
It was attached to the side (see Figure 2), and its deodorizing effect was judged by the subject's sense of smell 6 months after the start of use. The catalyst layer 7 has a geometric surface area of 1800 m'/a', a specific surface area of 120 m'/g, and a cell number of 210 cells/1n.
A ch2 honeycomb-shaped catalyst is used, and an activated carbon layer 1 is used.
No. 2 was formed into a honeycomb shape with a cell count of 200 cells/1 nch2.
さらに該脱臭装置1は人体感知センサを備えたものを利
用し、トイレ内に人間が入っているときに作動し人間が
出た数秒後に自動的に停止する構造とし、便器20内か
らの吸引風量は1分間光たり0.17+n’とし、また
オゾン発生濃度は0.5ppm、単位風量i n+3/
hr当たりの触媒接触表面積は0.035m2とした。Furthermore, the deodorizing device 1 is equipped with a human body detection sensor, and has a structure that starts when a person is in the toilet and automatically stops a few seconds after the person comes out, and the amount of suction air from inside the toilet bowl 20 is reduced. is 0.17+n' per minute of light, the ozone generation concentration is 0.5ppm, and the unit air volume is i n+3/
The catalyst contact surface area per hour was 0.035 m2.
5名の被験者によって脱臭効果の判定を行なったところ
、全員臭気を感じないという結果を得た。When the deodorizing effect was evaluated by five test subjects, all of them found that they did not feel any odor.
[発明の効果]
本発明によりオゾン触媒方法でも分解処理できなかった
臭気成分を吸着除去できる様になり、空気中の悪臭ガス
をほぼ完全に分解処理又は吸着除去できる様になった。[Effects of the Invention] According to the present invention, it has become possible to adsorb and remove odor components that cannot be decomposed even by the ozone catalyst method, and it has become possible to almost completely decompose or adsorb and remove malodorous gases in the air.
また活性炭層における悪臭成分の吸着除去は、オゾン・
触媒方法で処理できなかった成分に限られるので、該活
性炭層は長期にわたって吸着性能を持続でき交換や再生
のメンテナンスは少なくて済む。In addition, the adsorption and removal of malodorous components in the activated carbon layer is
Since the activated carbon layer is limited to components that cannot be treated by the catalytic method, the activated carbon layer can maintain its adsorption performance over a long period of time and requires less maintenance such as replacement or regeneration.
第1図は本発明に適用される脱臭装置の実施例を示す断
面説明図、第2図は第1図における脱臭装置の使用例を
示す説明図、第3図は脱臭装置の例を示す概略説明図で
ある。
1・・・脱臭装置 2・・・吸気口3・・・排気
口 4・・・通気路5・・・オゾン発生器
6・・・オゾン・悪臭成分混合室
7・・・触媒層 8・・・吸気ファンlO・・
・トランス 12・・・活性炭層20・・・便器
21・・・便座第1FIG. 1 is a cross-sectional explanatory diagram showing an example of the deodorizing device applied to the present invention, FIG. 2 is an explanatory diagram showing an example of use of the deodorizing device in FIG. 1, and FIG. 3 is a schematic diagram showing an example of the deodorizing device. It is an explanatory diagram. 1...Deodorizing device 2...Intake port 3...Exhaust port 4...Air passage 5...Ozone generator 6...Ozone/malodorous component mixing chamber 7...Catalyst layer 8...・Intake fan lO・・
・Transformer 12...Activated carbon layer 20...Toilet bowl 21...Toilet seat 1st
Claims (1)
た後、未分解臭気成分を前記触媒の下流側に設けた活性
炭層によって吸着除去することを特徴とする脱臭方法。A deodorizing method characterized by mixing malodorous gas with ozone, decomposing it in the presence of a catalyst, and then adsorbing and removing undecomposed malodorous components by an activated carbon layer provided downstream of the catalyst.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63293929A JPH02139017A (en) | 1988-11-21 | 1988-11-21 | Deodorizing process |
KR1019890002660A KR960000210B1 (en) | 1988-03-04 | 1989-03-03 | Method and apparatus for deodorizing toilet room |
EP89103776A EP0331192B1 (en) | 1988-03-04 | 1989-03-03 | Method and apparatus for deodorizing toilet room |
DE8989103776T DE68901201D1 (en) | 1988-03-04 | 1989-03-03 | METHOD AND DEVICE FOR DESODORING TOILET SPACES. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63293929A JPH02139017A (en) | 1988-11-21 | 1988-11-21 | Deodorizing process |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02139017A true JPH02139017A (en) | 1990-05-29 |
Family
ID=17800993
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63293929A Pending JPH02139017A (en) | 1988-03-04 | 1988-11-21 | Deodorizing process |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02139017A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007029270A (en) * | 2005-07-25 | 2007-02-08 | Daikin Ind Ltd | Deodorizing mechanism |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS539184A (en) * | 1976-07-13 | 1978-01-27 | Matsushita Electric Ind Co Ltd | Automatic unbalance correcting apparatus |
JPS58150414A (en) * | 1982-03-02 | 1983-09-07 | Mitsubishi Heavy Ind Ltd | Removal of malodor |
-
1988
- 1988-11-21 JP JP63293929A patent/JPH02139017A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS539184A (en) * | 1976-07-13 | 1978-01-27 | Matsushita Electric Ind Co Ltd | Automatic unbalance correcting apparatus |
JPS58150414A (en) * | 1982-03-02 | 1983-09-07 | Mitsubishi Heavy Ind Ltd | Removal of malodor |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007029270A (en) * | 2005-07-25 | 2007-02-08 | Daikin Ind Ltd | Deodorizing mechanism |
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