CN105597736A - Dioxin catalyst for production of cellular bricks - Google Patents
Dioxin catalyst for production of cellular bricks Download PDFInfo
- Publication number
- CN105597736A CN105597736A CN201610137604.XA CN201610137604A CN105597736A CN 105597736 A CN105597736 A CN 105597736A CN 201610137604 A CN201610137604 A CN 201610137604A CN 105597736 A CN105597736 A CN 105597736A
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- CN
- China
- Prior art keywords
- catalyst
- nanometer
- dioxin
- cellular
- production
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- 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.)
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- 239000003054 catalyst Substances 0.000 title claims abstract description 26
- 239000011449 brick Substances 0.000 title claims abstract description 24
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title abstract description 6
- 230000001413 cellular effect Effects 0.000 title abstract 4
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 claims abstract description 10
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 claims abstract description 10
- ZNOKGRXACCSDPY-UHFFFAOYSA-N tungsten trioxide Chemical compound O=[W](=O)=O ZNOKGRXACCSDPY-UHFFFAOYSA-N 0.000 claims abstract description 9
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000005543 nano-size silicon particle Substances 0.000 claims abstract description 4
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 2
- 238000006555 catalytic reaction Methods 0.000 abstract description 7
- 230000003197 catalytic effect Effects 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 2
- 238000004134 energy conservation Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000011943 nanocatalyst Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8668—Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—Tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/20—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
- B01J35/23—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Catalysts (AREA)
Abstract
The invention relates to a dioxin catalyst for production of cellular bricks. The dioxin catalyst is prepared from, by weight, 90% of nanometer titania, 2.5% of nanometer vanadium pentoxide, 4% of nanometer tungsten trioxide, 1% of nanometer molybdenum trioxide and 2.5% of nanosilicon dioxide. The catalyst is prepared from the nanometer base materials, the catalyst more easily and fully adheres to the cellular bricks, the catalytic effect is more obvious, the processing difficulty and cost of the cellular brick type catalyst are reduced, the requirement for the catalysis achieving environment is lowered, and therefore energy efficiency is improved and energy is saved.
Description
Technical field
The invention belongs to honeycomb brick produce and dioxin catalyst technical field, relate in particular to one forThe dioxin catalyst that honeycomb brick is produced.
Background technology
At present, in honeycomb brick production process in order to reduce the discharge of dioxin, row all can be to honeycomb brick timeImmersion, catalysis; This process needs to use dioxin catalyst, the catalyst doing on the market, allBe that the composition with catalyst is made into honeycomb brick completely, and the environment temperature that generation catalysis needs existMore than 400 DEG C, ours is the surface that nanocatalyst is attached to honeycomb brick, has both used honeycombThe area of brick maximizes, and reduces the consumption of catalyst simultaneously. Both reduced adding of honeycomb brick formula catalystWork difficulty and cost, reduce for the environmental requirement that realizes catalysis, thereby it is energy-conservation to reduce efficiency.
Summary of the invention
For solving the above-mentioned problems in the prior art, the invention provides a kind of for honeycomb brickWhen production more easily, stick to more fully the surface of honeycomb brick completely, consumption is few, catalytic effectSignificantly dioxin catalyst.
For solving the problems of the technologies described above, the present invention adopts following technical scheme:
A dioxin catalyst of producing for honeycomb brick, is prepared by following composition and percentage by weightForm: 90% nano titanium oxide, 2.5% nanometer vanadic anhydride, 4% nano tungsten trioxide,1% nanometer molybdenum trioxide and 2.5% nano silicon.
The invention has the beneficial effects as follows:
The present invention is by technique scheme, during for the production of honeycomb brick catalyst more easily, more abundantGround sticks to the surface of honeycomb brick completely, greatly reduces the consumption of catalyst, the catalytic effect of dioxinMore obvious, both reduced difficulty of processing and the cost of honeycomb brick, reduce for the environment of realizing catalysis and wantAsk, thereby it is energy-conservation to reduce efficiency.
The present invention, by adopting nanometer base material to make, can will just produce catalysis effect at 80 DEG C~90 DEG CReally, catalytic efficiency reaches 98%.
Detailed description of the invention
In order to make object of the present invention, technical scheme and advantage clearer, below in conjunction with enforcementExample, is further elaborated to the present invention. Should be appreciated that specific embodiment described hereinOnly, in order to explain the present invention, be not intended to limit the present invention.
A kind of dioxin catalyst of producing for honeycomb brick of the present invention, by following composition and heavyAmount percentage is prepared from: 90% nano titanium oxide (TiO2), 2.5% nanometer vanadic anhydride(V2O5), 4% nano tungsten trioxide (WO3), 1% nanometer molybdenum trioxide (MoO3) and 2.5%Nano silicon (SiO2)。
While utilizing dioxin Catalyst Production honeycomb brick of the present invention, first by dioxin catalyst withSolution mixes, is made into dioxin catalyst solution, then honeycomb brick is dipped in catalyst solution,Soak into, finally take out and dry.
Through experimental test, because dioxin catalyst of the present invention adopts said components and percentage by weight,Immersion process make catalyst more easily, stick to more fully the surface of honeycomb brick completely, andAt the temperature of 80 DEG C~90 DEG C, catalytic efficiency can reach 98%. Can greatly reduce like this consumption of catalyst,The catalytic effect of dioxin is more obvious, has both reduced difficulty of processing and the cost of honeycomb brick, reduce forRealize the environmental requirement of catalysis, thereby it is energy-conservation to reduce efficiency.
The above is the preferred embodiment of the present invention, it should be pointed out that general for the artLogical technical staff, under the premise without departing from the principles of the invention, can also make some improvement andRetouching, these improvements and modifications are also considered as protection scope of the present invention.
Claims (1)
1. a dioxin catalyst of producing for honeycomb brick, is characterized in that, by following composition andPercentage by weight is prepared from: 90% nano titanium oxide, 2.5% nanometer vanadic anhydride, 4%Nano tungsten trioxide, 1% nanometer molybdenum trioxide and 2.5% nano silicon.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610137604.XA CN105597736A (en) | 2016-03-10 | 2016-03-10 | Dioxin catalyst for production of cellular bricks |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610137604.XA CN105597736A (en) | 2016-03-10 | 2016-03-10 | Dioxin catalyst for production of cellular bricks |
Publications (1)
Publication Number | Publication Date |
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CN105597736A true CN105597736A (en) | 2016-05-25 |
Family
ID=55978402
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201610137604.XA Pending CN105597736A (en) | 2016-03-10 | 2016-03-10 | Dioxin catalyst for production of cellular bricks |
Country Status (1)
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CN (1) | CN105597736A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000000471A (en) * | 1998-04-16 | 2000-01-07 | Mitsubishi Heavy Ind Ltd | Waste gas treating catalyst, waste gas treatment and treating device |
CN1626277A (en) * | 2003-12-11 | 2005-06-15 | 西北化工研究院 | Catalyst for depriving dioxin in discharge gas from garbage furnace |
CN103495417A (en) * | 2013-09-30 | 2014-01-08 | 山东爱亿普环保科技有限公司 | Special ceramic catalyst for denitrification and dioxin removal of flue gas and preparation method thereof |
CN104671715A (en) * | 2015-01-26 | 2015-06-03 | 广东源盛生态环保科技有限公司 | Method for preparing light-weight protection wall by utilizing flying ash generated after garbage power |
CN104801296A (en) * | 2015-04-13 | 2015-07-29 | 宜兴市宜刚环保工程材料有限公司 | Novel dioxin removing catalyst and preparation method thereof |
-
2016
- 2016-03-10 CN CN201610137604.XA patent/CN105597736A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000000471A (en) * | 1998-04-16 | 2000-01-07 | Mitsubishi Heavy Ind Ltd | Waste gas treating catalyst, waste gas treatment and treating device |
CN1626277A (en) * | 2003-12-11 | 2005-06-15 | 西北化工研究院 | Catalyst for depriving dioxin in discharge gas from garbage furnace |
CN103495417A (en) * | 2013-09-30 | 2014-01-08 | 山东爱亿普环保科技有限公司 | Special ceramic catalyst for denitrification and dioxin removal of flue gas and preparation method thereof |
CN104671715A (en) * | 2015-01-26 | 2015-06-03 | 广东源盛生态环保科技有限公司 | Method for preparing light-weight protection wall by utilizing flying ash generated after garbage power |
CN104801296A (en) * | 2015-04-13 | 2015-07-29 | 宜兴市宜刚环保工程材料有限公司 | Novel dioxin removing catalyst and preparation method thereof |
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Application publication date: 20160525 |
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