JPH02284648A - Activated catalyst for deodorizing ozone - Google Patents
Activated catalyst for deodorizing ozoneInfo
- Publication number
- JPH02284648A JPH02284648A JP1105774A JP10577489A JPH02284648A JP H02284648 A JPH02284648 A JP H02284648A JP 1105774 A JP1105774 A JP 1105774A JP 10577489 A JP10577489 A JP 10577489A JP H02284648 A JPH02284648 A JP H02284648A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- ozone
- reducing agent
- reducing
- soln
- 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.)
- Granted
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 54
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 230000001877 deodorizing effect Effects 0.000 title claims abstract description 19
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 11
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 7
- 150000004706 metal oxides Chemical class 0.000 claims description 17
- 239000003638 chemical reducing agent Substances 0.000 abstract description 13
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 9
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 7
- 230000002829 reductive effect Effects 0.000 abstract description 6
- 239000011148 porous material Substances 0.000 abstract description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052804 chromium Inorganic materials 0.000 abstract description 2
- 239000011651 chromium Substances 0.000 abstract description 2
- 238000004898 kneading Methods 0.000 abstract description 2
- 229910052720 vanadium Inorganic materials 0.000 abstract description 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 abstract description 2
- 230000003197 catalytic effect Effects 0.000 abstract 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 abstract 1
- 230000004913 activation Effects 0.000 abstract 1
- 239000012190 activator Substances 0.000 abstract 1
- 229910002804 graphite Inorganic materials 0.000 abstract 1
- 239000010439 graphite Substances 0.000 abstract 1
- 229910052748 manganese Inorganic materials 0.000 abstract 1
- 239000011572 manganese Substances 0.000 abstract 1
- 229910052751 metal Inorganic materials 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 150000002739 metals Chemical class 0.000 abstract 1
- 239000002994 raw material Substances 0.000 abstract 1
- 238000001291 vacuum drying Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 12
- 235000019645 odor Nutrition 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 238000004332 deodorization Methods 0.000 description 3
- -1 gutphite Chemical compound 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- 235000013162 Cocos nucifera Nutrition 0.000 description 2
- 244000060011 Cocos nucifera Species 0.000 description 2
- AVXURJPOCDRRFD-UHFFFAOYSA-N Hydroxylamine Chemical compound ON AVXURJPOCDRRFD-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 229910052703 rhodium Inorganic materials 0.000 description 2
- 239000010948 rhodium Substances 0.000 description 2
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 241000272201 Columbiformes Species 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 235000003434 Sesamum indicum Nutrition 0.000 description 1
- 244000000231 Sesamum indicum Species 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 229910000428 cobalt oxide Inorganic materials 0.000 description 1
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical compound [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は活性化されたオゾン脱臭触媒に関し、特に下水
、し尿、ごみ焼却施設から発生する臭気をオゾン脱臭す
るに際して使用するに適した活性化オゾン脱臭触媒に関
する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an activated ozone deodorizing catalyst, particularly an activated ozone deodorizing catalyst suitable for use in ozone deodorizing of odors generated from sewage, human waste, and garbage incineration facilities. Regarding ozone deodorizing catalyst.
悪臭成分を気相中でオゾンによシ酸化分解するオゾン脱
臭(悪臭の除去)方法が既に提供されているが、(特公
昭63−39283号公報)この提案方法では、炭素質
材料からなる担体上に金属酸化物を担持させた触媒層を
複数居直列に配設し、かつ、該各層の前部にそれぞれオ
ゾン注入手段を設けることが特徴の1つになっている。An ozone deodorization (offensive odor removal) method has already been proposed in which odor components are oxidized and decomposed by ozone in the gas phase. One of the features is that a plurality of catalyst layers each carrying a metal oxide are arranged in series, and an ozone injection means is provided in front of each layer.
この提案方法でいう触媒とは、例えば粒状、破砕状また
は粉末状活性炭、グツファイト、炭素繊維などからなる
触媒担体上に、バナジウム、クロム、マンガン、鉄、コ
バルト、ニッケル、銅、銀、亜鉛などの金属酸化物の1
種以上を担持させたもので、必要に応じて白金、バヲジ
ウム、ロジウム、ルテニウムなどを助触媒としてこの金
属酸化物と共に担持させているものである。The catalyst used in this proposed method is, for example, a catalyst carrier made of granular, crushed or powdered activated carbon, gutphite, carbon fiber, etc. metal oxide 1
If necessary, platinum, barodium, rhodium, ruthenium, etc. are supported together with the metal oxide as a co-catalyst.
この提案方法では触れていないが、上記触媒を製造する
ためには、触媒活性金属酸化物と担体とを成形、乾燥後
、還元雰囲気条件下での焼成が必要にかり、高活性な触
媒を連続して安定製造するのは容易でない面があった。Although not mentioned in this proposed method, in order to produce the above catalyst, it is necessary to mold the catalytically active metal oxide and the carrier, dry it, and then sinter it under reducing atmosphere conditions, which allows continuous production of the highly active catalyst. However, it was not easy to produce it stably.
本発明は、上記技術水準に鑑み、従来のオゾン脱臭触媒
よυ高活性で、かつ、連続して安定した性能をもつオゾ
ン脱臭触媒を提供1〜ようとするものである。In view of the above-mentioned state of the art, the present invention aims to provide an ozone deodorizing catalyst which is more active than conventional ozone deodorizing catalysts and has continuously stable performance.
本発明は1種以上の金属酸化物を炭素質材料に担持して
なるオゾン脱臭触媒を、還元溶液で処理したのち乾燥し
てなることを特徴とする活性化オゾン脱臭触媒である。The present invention is an activated ozone deodorizing catalyst, which is obtained by treating an ozone deodorizing catalyst in which one or more metal oxides are supported on a carbonaceous material with a reducing solution and then drying the catalyst.
本発明でいう1種以上の金属酸化物を炭素質材料に担持
したオゾン脱臭触媒とは、粒状、破砕状または粉末状活
性炭、グクファイト、炭素繊維などからなる担体上に、
活性成分としてバナジウム、クロム、マンガン、鉄、コ
バ/I/l、ニッケル、銅、銀、亜鉛などの金属酸化物
の1種以上を担持させたもの、及び必要に応じて白金、
バッジラム、ロジウム、ルテニウムfr、トを助触媒と
して前記金属酸化物と共に担持させたものを成形、乾燥
、焼成してなるものをいう。The ozone deodorizing catalyst in which one or more metal oxides are supported on a carbonaceous material as used in the present invention refers to an ozone deodorizing catalyst in which one or more metal oxides are supported on a carbonaceous material, and an ozone deodorizing catalyst in which one or more metal oxides are supported on a carbonaceous material is a
One or more metal oxides such as vanadium, chromium, manganese, iron, Koba/I/L, nickel, copper, silver, and zinc are supported as active ingredients, and if necessary, platinum,
It refers to a product obtained by molding, drying, and calcining a product in which badge rhum, rhodium, ruthenium fr, and to are supported together with the metal oxides mentioned above as cocatalysts.
本発明触媒は上記公知のオゾン脱臭触媒を還元溶液で処
理した後、乾燥したものであるが、還元溶液とはホルム
ア/l/ダヒド水溶液、アセトアルデヒドなどの低沸点
アルデヒド水溶液、ヒドロキシルアミン、アスコロビン
酸などの水溶性還元剤が用いられる。還元溶液処理後の
乾燥は酸化を防ぐため、−殻内に100〜180 ’C
。The catalyst of the present invention is obtained by treating the above-mentioned known ozone deodorizing catalyst with a reducing solution and then drying it. The reducing solution is a formala/l/dahyde aqueous solution, a low boiling point aldehyde aqueous solution such as acetaldehyde, hydroxylamine, ascobic acid, etc. A water-soluble reducing agent is used. Drying after the reducing solution treatment is carried out at -100-180'C inside the shell to prevent oxidation.
.
好ましくは105=150°Cで行うのが好−!、I−
く、触媒細孔内に残留する還元溶液を除去するためにも
減圧下で行うのが好ましい。Preferably it is carried out at 105=150°C! ,I-
In addition, it is preferable to carry out the reaction under reduced pressure in order to remove the reducing solution remaining in the catalyst pores.
前記した1種以上の金属酸化物を炭素質材料に担持した
触媒を還元溶液で処理することによって、前記触媒担体
に担持した金属酸化物は部分還元され、このような状態
になった触媒は悪臭成分を酸化分解するオゾン脱臭法に
おける有効な触媒として作用する。By treating the catalyst in which one or more of the metal oxides described above supported on a carbonaceous material with a reducing solution, the metal oxide supported on the catalyst carrier is partially reduced, and the catalyst in such a state has a bad odor. Acts as an effective catalyst in ozone deodorization methods that oxidize and decompose components.
以下、本発明の活性化オゾン脱臭触媒の製造例の概要を
第1図によって説明する。第1図において、M、は触媒
活性体となる金属酸化物の出発原料、M、は触媒担体、
M、は還元剤溶液、鳩は製品、1は従来触媒製造工程、
2は還元処理工程、3は乾燥工程を示す。Hereinafter, an outline of a manufacturing example of the activated ozone deodorizing catalyst of the present invention will be explained with reference to FIG. In FIG. 1, M is a starting material for a metal oxide that becomes a catalyst active body, M is a catalyst carrier,
M is the reducing agent solution, pigeon is the product, 1 is the conventional catalyst manufacturing process,
2 indicates a reduction treatment step, and 3 indicates a drying step.
触媒活性体出発原料M、と触媒担体M、を含浸法又は混
練法によって成形後(成形はベレット状、ハニカム状、
繊維布状いづれでもよい)、乾燥・焼成する従来触媒製
造工程1を経たのち、還元工程2において還元処理する
。ここでは、還元剤を含む溶液中に上記触媒製造工程1
を径由した触媒を浸漬、十分にかきまぜI7て還元処理
操作を行なうととKある。還元剤としては、例えばホμ
ムアμ/デヒド水溶液、アセトアルデヒドの低沸点ア/
l/デヒド類、ヒドロキシアミン、アスコロビン酸など
、とくに水溶性還元剤が好ましい、、また、還元剤の濃
度は(11〜10wt%、好ましくは0.5〜5 wt
%がよく、触媒重量に列して1〜5倍(N量)、好まし
くは1〜3倍がよい。溶液温度は室温でよいが、効果を
高めるため、50〜40°Cに上げること本できる。た
だし、その場合は還元剤の蒸発が起ることもあるので注
意を要す。浸漬時間は適宜、金属酸化物の還元処理状態
に合せて調整することになるが、概ね1〜10時間であ
る。After molding the catalyst active starting material M and the catalyst carrier M by an impregnation method or a kneading method (the molding is performed in a pellet shape, a honeycomb shape,
After passing through the conventional catalyst production step 1 of drying and firing (either in the form of fiber cloth), it is subjected to reduction treatment in the reduction step 2. Here, the above catalyst manufacturing step 1 is added to a solution containing a reducing agent.
The catalyst is immersed and thoroughly stirred to carry out the reduction treatment. As the reducing agent, for example,
Mua μ / Dehyde aqueous solution, low boiling point a of acetaldehyde /
Water-soluble reducing agents such as l/dehydes, hydroxyamines, ascobic acid, etc. are particularly preferable, and the concentration of the reducing agent is (11 to 10 wt%, preferably 0.5 to 5 wt%).
%, preferably 1 to 5 times (N amount), preferably 1 to 3 times the weight of the catalyst. The solution temperature may be at room temperature, but it can be raised to 50 to 40°C to enhance the effect. However, care must be taken in this case as evaporation of the reducing agent may occur. The immersion time will be adjusted as appropriate depending on the state of the reduction treatment of the metal oxide, but is approximately 1 to 10 hours.
つぎに、還元処理した触媒は100−180’C%好ま
しくは105〜150°Cの雰囲気下で乾燥する。乾燥
の促進、及び触媒細孔内に残留する還元剤を迅速に1離
脱するためにも減圧乾燥操作が好ましい。Next, the reduced catalyst is dried in an atmosphere of 100-180'C%, preferably 105-150C. Drying under reduced pressure is also preferred in order to accelerate drying and quickly remove the reducing agent remaining in the catalyst pores.
第2図に、ホルマリン水溶液を還元剤と1〜だときの効
果の一例を示す。触媒は粒状ヤシガラ活性炭を担体とし
、コバ/1/)酸化物を担持1.たものである。還元剤
濃度の増加に伴いオゾン分解効果(脱臭効果と比例する
)が増大する。1〔実施例〕
ヤシガフ活性炭(4〜6鴎φX4〜10鱈I])を担体
として、酸化コバルトを4wt%担持した触媒を、2
wt%ホルマリン水溶液に約2時間浸漬したのち取出し
て、水切りし、130°Cで水分およびホルマリン臭が
なくなる壕で減圧乾燥した。FIG. 2 shows an example of the effect when an aqueous formalin solution is mixed with a reducing agent. The catalyst uses granular coconut shell activated carbon as a carrier, and supports 1. It is something that As the reducing agent concentration increases, the ozone decomposition effect (proportional to the deodorizing effect) increases. 1 [Example] A catalyst in which 4 wt % of cobalt oxide was supported on coconut activated carbon (4 to 6 φX 4 to 10 cod I) was
After being immersed in a wt% formalin aqueous solution for about 2 hours, it was taken out, drained, and dried under reduced pressure at 130°C in a trench to eliminate moisture and formalin odor.
その後、オゾン濃度10 ppmを含む空気を、上記触
[38si!充てんした反応管に、S■=I(−1
toooo の条件下で通して出口オゾン濃度を測
定し、オゾン分解率を求めた。Thereafter, air containing an ozone concentration of 10 ppm was introduced into the air [38si! The ozone concentration at the outlet was measured by passing the mixture through the filled reaction tube under the condition of S■=I(-1 toooo), and the ozone decomposition rate was determined.
その結果、オゾン分解率は9995%であった。これに
対し、還元処理をしない触媒のオゾン分解率は99.8
5%であり、両者に差が認められた。As a result, the ozone decomposition rate was 9995%. In contrast, the ozone decomposition rate of the catalyst without reduction treatment was 99.8.
5%, and a difference was observed between the two.
上記実施例は活性成分として酸化ゴバルトを使用したも
のであるが、その他前記活性触媒成分としてあげた金属
酸化物も該実施例とはソ同様な結果が得られた。Although the above example used gobalt oxide as the active component, similar results were obtained with other metal oxides listed as the active catalyst component.
戻素質材料触謀担体に金属酸化物を担持した触媒を、還
元溶液にて処理することによって、触媒の高活性化を図
ることができ、恕臭成分を酸化分解するオゾン脱臭法に
おける有効な触媒とすることができた。By treating a catalyst in which a metal oxide is supported on a catalyst carrier with a reducing solution, the catalyst can be highly activated, making it an effective catalyst in the ozone deodorization method that oxidizes and decomposes odor components. I was able to do this.
第1図は本発明の活性化オゾン脱臭触媒の製造例の工程
図、第2図は本発明触媒の還元溶液処理の効果を示す図
表である。FIG. 1 is a process diagram of an example of manufacturing the activated ozone deodorizing catalyst of the present invention, and FIG. 2 is a chart showing the effect of treating the catalyst of the present invention with a reducing solution.
Claims (1)
ン脱臭触媒を、還元溶液で処理したのち乾燥してなるこ
とを特徴とする活性化オゾン脱臭触媒。An activated ozone deodorizing catalyst characterized in that it is obtained by treating an ozone deodorizing catalyst comprising one or more metal oxides supported on a carbonaceous material with a reducing solution and then drying the catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1105774A JP2615196B2 (en) | 1989-04-27 | 1989-04-27 | Method for producing activated ozone deodorizing catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1105774A JP2615196B2 (en) | 1989-04-27 | 1989-04-27 | Method for producing activated ozone deodorizing catalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02284648A true JPH02284648A (en) | 1990-11-22 |
JP2615196B2 JP2615196B2 (en) | 1997-05-28 |
Family
ID=14416508
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1105774A Expired - Lifetime JP2615196B2 (en) | 1989-04-27 | 1989-04-27 | Method for producing activated ozone deodorizing catalyst |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2615196B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0643014A1 (en) * | 1993-09-14 | 1995-03-15 | Kuraray Chemical Co., Ltd. | Deodorant comprising metal oxide-carrying activated carbon |
CN111617767A (en) * | 2020-06-03 | 2020-09-04 | 南京神克隆水务有限公司 | Ozone oxidation catalyst for wastewater treatment and preparation method thereof |
CN112264010A (en) * | 2020-10-26 | 2021-01-26 | 珠海格力电器股份有限公司 | Catalyst for normal-temperature decomposition of formaldehyde and preparation method thereof |
CN116371419A (en) * | 2023-04-21 | 2023-07-04 | 中南大学 | Microbial carbon-supported manganese-cobalt catalyst and preparation method and application thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5216875A (en) * | 1975-07-30 | 1977-02-08 | Hitachi Ltd | Splash prevnter for rotational dryer |
-
1989
- 1989-04-27 JP JP1105774A patent/JP2615196B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5216875A (en) * | 1975-07-30 | 1977-02-08 | Hitachi Ltd | Splash prevnter for rotational dryer |
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EP0643014A1 (en) * | 1993-09-14 | 1995-03-15 | Kuraray Chemical Co., Ltd. | Deodorant comprising metal oxide-carrying activated carbon |
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CN111617767B (en) * | 2020-06-03 | 2023-08-29 | 南京神克隆科技有限公司 | Ozone oxidation catalyst for wastewater treatment and preparation method thereof |
CN112264010A (en) * | 2020-10-26 | 2021-01-26 | 珠海格力电器股份有限公司 | Catalyst for normal-temperature decomposition of formaldehyde and preparation method thereof |
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