CN107413393A - A kind of wear-resistant composite denitration catalyst and preparation method for glass furnace - Google Patents
A kind of wear-resistant composite denitration catalyst and preparation method for glass furnace Download PDFInfo
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- CN107413393A CN107413393A CN201710488054.0A CN201710488054A CN107413393A CN 107413393 A CN107413393 A CN 107413393A CN 201710488054 A CN201710488054 A CN 201710488054A CN 107413393 A CN107413393 A CN 107413393A
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- 239000003054 catalyst Substances 0.000 title claims abstract description 59
- 239000011521 glass Substances 0.000 title claims abstract description 25
- 239000002131 composite material Substances 0.000 title claims abstract description 24
- 238000002360 preparation method Methods 0.000 title claims abstract description 23
- 239000000919 ceramic Substances 0.000 claims abstract description 47
- 230000001413 cellular effect Effects 0.000 claims abstract description 16
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 9
- 239000010935 stainless steel Substances 0.000 claims abstract description 9
- 239000003795 chemical substances by application Substances 0.000 claims description 21
- 239000000843 powder Substances 0.000 claims description 18
- 239000000314 lubricant Substances 0.000 claims description 17
- 239000000654 additive Substances 0.000 claims description 10
- 230000000996 additive effect Effects 0.000 claims description 10
- 238000001125 extrusion Methods 0.000 claims description 10
- 238000001914 filtration Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 7
- 238000004513 sizing Methods 0.000 claims description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 6
- 238000004898 kneading Methods 0.000 claims description 5
- 235000021355 Stearic acid Nutrition 0.000 claims description 4
- 238000000498 ball milling Methods 0.000 claims description 4
- 238000001354 calcination Methods 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 4
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical group CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 4
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 4
- 239000008117 stearic acid Substances 0.000 claims description 4
- 239000000758 substrate Substances 0.000 claims description 4
- 239000005995 Aluminium silicate Substances 0.000 claims description 3
- 229920000742 Cotton Polymers 0.000 claims description 3
- 229920001131 Pulp (paper) Polymers 0.000 claims description 3
- 238000007605 air drying Methods 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 235000012211 aluminium silicate Nutrition 0.000 claims description 3
- CNLWCVNCHLKFHK-UHFFFAOYSA-N aluminum;lithium;dioxido(oxo)silane Chemical compound [Li+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O CNLWCVNCHLKFHK-UHFFFAOYSA-N 0.000 claims description 3
- DLHONNLASJQAHX-UHFFFAOYSA-N aluminum;potassium;oxygen(2-);silicon(4+) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Al+3].[Si+4].[Si+4].[Si+4].[K+] DLHONNLASJQAHX-UHFFFAOYSA-N 0.000 claims description 3
- 229910052849 andalusite Inorganic materials 0.000 claims description 3
- 239000004927 clay Substances 0.000 claims description 3
- 229910052878 cordierite Inorganic materials 0.000 claims description 3
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 claims description 3
- 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 claims description 3
- 239000003365 glass fiber Substances 0.000 claims description 3
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 claims description 3
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 claims description 3
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 3
- 238000007493 shaping process Methods 0.000 claims description 3
- 229910052642 spodumene Inorganic materials 0.000 claims description 3
- 239000004408 titanium dioxide Substances 0.000 claims description 3
- 235000015112 vegetable and seed oil Nutrition 0.000 claims description 3
- 239000008158 vegetable oil Substances 0.000 claims description 3
- WSNKEJIFARPOSQ-UHFFFAOYSA-N 3-[4-(aminomethyl)-6-(trifluoromethyl)pyridin-2-yl]oxy-N-(1-benzothiophen-2-ylmethyl)benzamide Chemical compound NCC1=CC(=NC(=C1)C(F)(F)F)OC=1C=C(C(=O)NCC2=CC3=C(S2)C=CC=C3)C=CC=1 WSNKEJIFARPOSQ-UHFFFAOYSA-N 0.000 claims description 2
- RGPUVZXXZFNFBF-UHFFFAOYSA-K diphosphonooxyalumanyl dihydrogen phosphate Chemical compound [Al+3].OP(O)([O-])=O.OP(O)([O-])=O.OP(O)([O-])=O RGPUVZXXZFNFBF-UHFFFAOYSA-K 0.000 claims description 2
- 238000007654 immersion Methods 0.000 claims description 2
- 230000001404 mediated effect Effects 0.000 claims description 2
- 239000010705 motor oil Substances 0.000 claims description 2
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 2
- 150000002910 rare earth metals Chemical class 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 claims 8
- RSWGJHLUYNHPMX-UHFFFAOYSA-N 1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylic acid Chemical compound C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims 1
- 241000256844 Apis mellifera Species 0.000 claims 1
- 229910000831 Steel Inorganic materials 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 239000010959 steel Substances 0.000 claims 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 10
- 239000003546 flue gas Substances 0.000 abstract description 10
- 238000005299 abrasion Methods 0.000 abstract description 7
- 239000000428 dust Substances 0.000 abstract description 5
- 230000007423 decrease Effects 0.000 abstract description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 12
- 241000264877 Hippospongia communis Species 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000002779 inactivation Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- -1 nitrogen-containing compound Chemical class 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000007866 anti-wear additive Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000003906 humectant Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
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- 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
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
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- 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
- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8628—Processes characterised by a specific catalyst
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- 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
- B01D53/96—Regeneration, reactivation or recycling of reactants
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- 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
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/16—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay
- C04B35/18—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay rich in aluminium oxide
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Abstract
The present invention is a kind of wear-resistant ceramic composite denitration catalyst for glass furnace and preparation method thereof, it is characterized in that termination position is wear-resisting Extruded Monolithic Celluar Ceramics, described main body section is wear-resisting cellular catalyst, both are combined with each other by being bonded hardening mud layer adhesion one in surrounding using stainless steel case nesting.It is mainly used in the denitrification apparatus of glass furnace, is applicable to the denitration of 250 ~ 400 DEG C wide temperature high-dust flue gas, termination position Extruded Monolithic Celluar Ceramics abrasion resistance properties are significantly better than traditional cellular catalyst, and overall denitration performance does not decline.
Description
Technical field
The invention belongs to industrial energy saving, emission abatement device technical field, and in particular to a kind of for the wear-resisting of glass furnace
Damage Ceramic Composite denitrating catalyst and preparation method thereof.
Background technology
Nitrogen oxides in air(NOx)A kind of common atmosphere pollution, it can not only cause acid rain, photochemical fog,
Earth's surface water eutrophication etc. destroys a series of problems of ecological environment, while also entail dangers to human health.Therefore, control in air
NOx discharge causes the concern in the whole world, and China is also classified as the emphasis in current atmospheric environment protection.
Research finds NO during fuel combustionxGeneration:First, nitrogen during burning in air is oxidized and generated at high temperature
Nitrogen oxides, second, the nitrogen that the nitrogen-containing compound in fuel decomposites at high temperature is oxidized to nitrogen oxides, glassware life
The flue gas discharged during production contains 3000-7000ppm nitrogen oxides.Its discharge capacity is only second to thermal power plant, row
Enter one of source of atmospheric pollution, China's glass furnace also generates substantial amounts of NO while promoting economic developmentx。
Reduce NOxDischarge has two approach of denitrating flue gas after Combustion Process Control and burning.In actual production, low NOx combustions
Burning technology efficiency is low, and mainly uses gas denitrifying technology.At present, the SCR denitration technology in gas denitrifying technology has denitration
The advantages that rate is high (can be more than 90%), and selectivity is good, and technology maturation is reliable, turn into the main flow of glass furnace denitration.
The part of most critical is catalyst in SCR denitration system, and glass furnace fume dust content is higher, is flown in flue gas
Ash particle rapid shock catalyst duct, in the lower flue gas that works long hours abrasion of the flying dust to catalyst catalyst mould mainly occurs
The end portion of block, corresponding end wear is the most serious, and growth over time, and catalyst module can be shorter and shorter, makes
The service life of catalyst is greatly reduced and further occurs and cavity and cave in, reduce denitration efficiency.
Although traditional honeycomb type denitrification catalyst is handled using the termination hardening bath of impregnation of phosphoric acid aluminum dihydrogen(Publication number:
CN 103316717 A), but it is also more serious using wearing under the flue gas of high dust-laden, have a strong impact on service life;Or in material
Antiwear additive SiC is added in material formula(Publication number:CN 106311301 A), but due to SiC powder material and in catalyst calcination
At a temperature of can not be firmly combined with, still have that compressive resistance is not high, used under the flue gas of high dust-laden, denitrating catalyst also can be gradual
It is worn.
Abrasion and flue gas flow rate and dust concentration, catalyst abrasion position etc. have certain relation.Therefore, invention is a kind of
Thus glass furnace is produced with the technical barrier that wear-resistant composite denitration catalyst is that this area is badly in need of solving at this stage, the present invention
It is raw.
The content of the invention
The technical problems to be solved by the invention are to provide a kind of wear-resistant ceramic composite denitration for glass furnace and urged
Agent and preparation method thereof.It is not high to solve existing denitrating catalyst anti-wear performance, decay resistance, it is easily long-pending during use
The technical problems such as ash blocks, the small heat exchange efficiency of specific surface area is low, service life is short.In glass furnace denitration device, with one kind
Wear-resistant ceramic composite can replace existing denitrating catalyst termination hardening position, by the simple cleanings of Bu Fan factories again
It is raw, the cost effective cleaning and regeneration of inactivation denitrating catalyst can be realized.
To achieve these goals, the technical solution used in the present invention is:A kind of wear-resistant pottery for glass furnace
Porcelain composite denitration catalyst and preparation method thereof, wear-resistant ceramic composite denitration catalyst include termination position, main body section, glued
Connect hardening mud layer, stainless steel case connection combines;Described termination position is wear-resisting Extruded Monolithic Celluar Ceramics, and there is positioning lower end
Raised line;Described main body section is wear-resisting cellular catalyst, and there is detent upper end;The lower end at the termination position and main body
The upper end at position is equipped with stainless steel case by being bonded hardening mud layer adhesion one, the bonding hardening mud layer surrounding.
Preferably, the bonding hardening mud layer uses aluminium dihydrogen phosphate, the immersion mixing of lucium active component
Formed.
Preferably, the termination position uses wear-resisting Extruded Monolithic Celluar Ceramics, including step is produced by below:
1)Wear-resisting Extruded Monolithic Celluar Ceramics include inorganic powder and additive, and the additive includes solid-state adhesion agent, lubricant,
Organic plasticising NMF;
Inorganic powder percetage by weight as shared by each raw material is:Andalusite 10 ~ 50%, cordierite 10 ~ 30%, spodumene 10 ~
30%th, white fused alumina 5 ~ 10%, potassium feldspar 1 ~ 10%, kaolin 1 ~ 10%, flint clay 5 ~ 35%;The weight of above-mentioned inorganic powder is with 100 parts
Meter, the agent of addition solid-state adhesion is 3 ~ 7 parts, 2 ~ 6 parts of lubricant, 0.5 ~ 2 part of organic plasticising NMF.
2)The preparation of wear-resisting Extruded Monolithic Celluar Ceramics:Ball milling, kneading, old obtained pug are molded by extruder, obtained
To honeycomb ceramics base substrate;Hot-air kiln dryness finalization is placed on after microwave is shaped;Burnt till by 1300 ~ 1350 DEG C, obtain termination
The honeycomb ceramic heat accumulator material at position.
Preferably, described wear-resisting Extruded Monolithic Celluar Ceramics are placed on sizing in heated-air drying kiln and dried, initial sizing temperature
65 DEG C of degree, 6 ~ 12h of drying time;The power of microwave sizing microwave oven is 5 ~ 10kW, and frequency is 2450MHz ± 50MHz.
The preparation of wear-resisting Extruded Monolithic Celluar Ceramics:Ball milling, kneading, old obtained pug are molded by extruder, obtained
Honeycomb ceramics base substrate;Hot-air kiln dryness finalization is placed on after microwave is shaped;Burnt till by 1300 ~ 1350 DEG C, obtain end head
The honeycomb ceramic heat accumulator material of position.
Preferably, solid-state adhesion agent is HPMC, CMC one or more mixing in the wear-resisting Extruded Monolithic Celluar Ceramics
Thing.Organic lubricant is vegetable oil, stearic acid, one or more mixtures of synthetic motor oil.Organic plasticising NMF be PEO,
PVA one or more mixtures.
Preferably, the wear-resisting cellular catalyst, its production stage are as follows:
1)Wear-resisting cellular catalyst includes inorganic powder and additive, and the additive includes solid-state adhesion agent, lubricant,
Organic plasticising NMF;
Inorganic powder percetage by weight as shared by each raw material is:Titanium dioxide 70-90%, montmorillonite 1-15%, rare earth mix
Compound 1-10%, glass fibre 1-5%, wood pulp cotton 1-5%;The weight of above-mentioned inorganic powder adds solid-state adhesion in terms of 100 parts
Agent is 0.5 ~ 5 part, 0.5 ~ 5 part of lubricant, 0.5 ~ 2 part of organic plasticising NMF.
2)The preparation of wear-resisting cellular catalyst:Kneading will be stirred, the vacuum equipped with mould is passed through in old, pre-filtering
Extruder shaping extrusion, is made the wet base of catalyst;Wherein old more than 24h;Pre-filtering uses specification 1 × 4mm or 0.8 × 3mm
Stainless steel filtering net;By hot-air kiln dryness finalization, then by 600 DEG C of calcinings, the wear-resisting honeycomb fashion for obtaining main body section is urged
Agent.
Preferably, the extrusion pressure of the vacuum-extruder is 3 ~ 6MPa, 35 DEG C of extrusion temperature <, extrusion vacuum-
0.09MPa。
Preferably, the solid-state adhesion agent is CMC, the organic lubricant is stearic acid, organic plasticising moisturizing
Agent is PEO.
The wear-resistant ceramic composite denitration catalyst of the present invention, is mainly used in the denitrification apparatus of glass furnace, applicable
In the denitration of 250 ~ 400 DEG C wide temperature high-dust flue gas, termination position Extruded Monolithic Celluar Ceramics abrasion resistance properties are significantly better than tradition
Cellular catalyst, and overall denitration performance does not decline.Because termination position abrasion resistance properties are good, pass through the letter of Bu Fan factories
Single cleaning and regeneration, the cost effective cleaning and regeneration of inactivation denitrating catalyst can be realized.Ceramic Composite denitrating catalyst of the present invention
Have the advantages that cost is low, service life is long, catalytic activity is high, wearability is good.It can be additionally used in the industries such as electric power, metallurgy, petrochemical industry
Denitrating flue gas, have wide range of applications, environment protection significance is great.
Brief description of the drawings
Structural representation when being perpendicular positioning of the present invention shown in Fig. 1.
Embodiment
For a better understanding of the present invention, with reference to embodiment, technical scheme is made further
Specific description.
As shown in figure 1, a kind of wear-resistant ceramic composite denitration catalyst for glass furnace and preparation method thereof, wear-resisting
Damaging Ceramic Composite denitrating catalyst includes termination position 1, main body section 2, bonding hardening mud layer 3, the connection combination of stainless steel case 4
Form, its appearance and size is 150mm × 150mm, 700 ~ 800mm of total height, termination position height 45mm.Termination position 1 is resistance to
Extruded Monolithic Celluar Ceramics are ground, there is positioning convex strip 11 lower end.Main body section 2 is wear-resisting cellular catalyst, and there is detent its upper end
21.Both can prevent that airflow hole inconsistent phenomenon occurs between termination position 1 and main body section 2 with accurate positioning, hard by being bonded
Change the adhesion of mud layer 3 one, and be combined with each other in surrounding using the nesting of stainless steel case 4.
Termination position 1 is as follows using wear-resisting Extruded Monolithic Celluar Ceramics production stage:
1)Inorganic powder percetage by weight as shared by each raw material is in wear-resisting Extruded Monolithic Celluar Ceramics:Andalusite 15%, cordierite 15%,
Spodumene 15%, white fused alumina 15%, potassium feldspar 10%, kaolin 10%, flint clay 20%;The weight of above-mentioned inorganic powder is with 100 parts
Meter, the agent of addition solid-state adhesion is 3.5 parts, 5 parts of lubricant, 1 part of organic plasticising NMF.
2)The preparation of wear-resisting Extruded Monolithic Celluar Ceramics:Ball milling, kneading, old obtained pug are molded by extruder, obtained
To honeycomb ceramics base substrate;Hot-air kiln dryness finalization is placed on after microwave is shaped;Burnt till by 1300 ~ 1350 DEG C, obtain termination
The honeycomb ceramic heat accumulator material at position.Described ceramic honey comb production stage:It is placed on sizing in heated-air drying kiln and dries, just
65 DEG C of beginning setting temperature, 6 ~ 12h of drying time;The power of microwave sizing microwave oven be 5kW, frequency for 2450MHz ±
50MHz;Solid-state adhesion agent HPMC is 3.5 parts;Organic lubricant vegetable oil is 4 parts;Organic plasticising NMF PEO is 1 part.Through surveying
Examination, the compression strength of honeycomb ceramic heat accumulator is 26~29MPa, bulk density is 2.1~2.2g/cm3, wearability be
7.6cm3, meet performance requirement of the glass furnace with wear-resistant composite denitration catalyst termination position.
Main body section 2 is as follows using wear-resisting cellular catalyst production stage:
1)Wear-resisting cellular catalyst includes inorganic powder and additive, and the additive includes solid-state adhesion agent, lubricant,
Organic plasticising NMF;
Inorganic powder percetage by weight as shared by each raw material is:Titanium dioxide 75%, montmorillonite 10%, lucium
10%th, glass fibre 2.5%, wood pulp cotton 2.5%;For the weight of above-mentioned inorganic powder in terms of 100 parts, it is 1 to add solid-state adhesion agent
Part, 1 part of lubricant, 1 part of organic plasticising NMF.Solid-state adhesion agent is CMC, and organic lubricant is stearic acid, and organic plasticising is protected
Humectant is PEO.
2)The preparation of wear-resisting cellular catalyst:Stirring is mediated, old, pre-filtering passes through the vacuum equipped with mould
Extruder shaping extrusion, is made the wet base of catalyst;By hot-air kiln dryness finalization;By 600 DEG C of calcinings, main body section is obtained
Wear-resisting cellular catalyst.The old time is more than 24h;Pre-filtering is filtered using specification 1 × 4mm or 0.8 × 3mm stainless steel
Net;The extrusion pressure of vacuum-extruder is 3 ~ 6MPa, 35 DEG C of extrusion temperature <, extrudes vacuum -0.09MPa.After tested, it is wear-resisting
The compression strength of cellular catalyst is 4~5MPa, 0.05 ~ 0.10 %/kg of hardening abrasion, it is contemplated that the longevity of catalyst is 2 ~ 3
Year, meet performance requirement of the glass furnace with wear-resistant composite denitration catalyst body position.
Finally it is pointed out that above embodiment is only the more representational example of the present invention.Obviously, it is of the invention
Above-mentioned embodiment is not limited to, there can also be many deformations.Every technical spirit according to the present invention specific reality to more than
Any simple modification, equivalent change and modification that the mode of applying is made, it is considered as belonging to protection scope of the present invention.
Claims (9)
1. a kind of wear-resistant ceramic composite denitration catalyst for glass furnace and preparation method thereof, wear-resistant ceramic is compound de-
Denox catalyst includes termination position, main body section, bonding hardens mud layer, stainless steel case connection combines, it is characterised in that
Described termination position is wear-resisting Extruded Monolithic Celluar Ceramics, and there is positioning convex strip lower end, and described main body section is that wear-resisting honeycomb fashion is urged
Agent, upper end have detent, the lower end at the termination position and the upper end of main body section to harden mud layer adhesion by being bonded
One, the bonding hardening mud layer surrounding are equipped with stainless steel case.
It is 2. according to claim 1 a kind of for the wear-resistant ceramic composite denitration catalyst of glass furnace and its preparation side
Method, it is characterised in that the bonding hardening mud layer is mixed to form using aluminium dihydrogen phosphate, the immersion of lucium active component.
It is 3. according to claim 1 a kind of for the wear-resistant ceramic composite denitration catalyst of glass furnace and its preparation side
Method, it is characterised in that the wear-resisting Extruded Monolithic Celluar Ceramics, including step is produced by below:
1)Wear-resisting Extruded Monolithic Celluar Ceramics include inorganic powder and additive, and the additive includes solid-state adhesion agent, lubricant,
Organic plasticising NMF;
Inorganic powder percetage by weight as shared by each raw material is:Andalusite 10 ~ 50%, cordierite 10 ~ 30%, spodumene 10 ~
30%th, white fused alumina 5 ~ 10%, potassium feldspar 1 ~ 10%, kaolin 1 ~ 10%, flint clay 5 ~ 35%;The weight of above-mentioned inorganic powder is with 100 parts
Meter, the agent of addition solid-state adhesion is 3 ~ 7 parts, 2 ~ 6 parts of lubricant, 0.5 ~ 2 part of organic plasticising NMF;
2)The preparation of wear-resisting Extruded Monolithic Celluar Ceramics:Ball milling, kneading, old obtained pug are molded by extruder, obtain honeybee
Nest body base substrate;Hot-air kiln dryness finalization and drying are placed on after microwave is shaped;Burn till, held by 1300 ~ 1350 DEG C
The honeycomb ceramic heat accumulator material of head position.
It is 4. described a kind of for the wear-resistant ceramic composite denitration catalyst of glass furnace and its preparation according to claim 1 or 3
Method, it is characterised in that described wear-resisting Extruded Monolithic Celluar Ceramics are placed on sizing in heated-air drying kiln and dried, initial setting temperature
65 DEG C, 6 ~ 12h of drying time;The power of microwave sizing microwave oven is 5 ~ 10kW, and frequency is 2450MHz ± 50MHz.
It is 5. according to claim 3 a kind of for the wear-resistant ceramic composite denitration catalyst of glass furnace and its preparation side
Method, it is characterised in that solid-state adhesion agent is HPMC, CMC one or more mixtures, and the organic lubricant is vegetable oil, firmly
One or more mixtures of resin acid, synthetic motor oil;Organic plasticising NMF is PEO, PVA one or more mixing
Thing.
It is 6. a kind of for the wear-resistant ceramic composite denitration catalyst of glass furnace and its preparation side according to claim 1
Method, it is characterised in that the wear-resisting cellular catalyst, including step is produced by below:
1)Wear-resisting cellular catalyst includes inorganic powder and additive, and the additive includes solid-state adhesion agent, lubricant,
Organic plasticising NMF;
Inorganic powder percetage by weight as shared by each raw material is:Titanium dioxide 70-90%, montmorillonite 1-15%, rare earth mix
Compound 1-10%, glass fibre 1-5%, wood pulp cotton 1-5%;The weight of above-mentioned inorganic powder adds solid-state adhesion in terms of 100 parts
Agent is 0.5 ~ 5 part, 0.5 ~ 5 part of lubricant, 0.5 ~ 2 part of organic plasticising NMF;
2)The preparation of wear-resisting cellular catalyst:Stirring is mediated, old, pre-filtering is passed through equipped with the shaping of mould vacuum-extruder
Extrusion, the wet base of catalyst is made;By hot-air kiln dryness finalization;By 600 DEG C of calcinings, the wear-resisting honeycomb of main body section is obtained
Formula catalyst.
It is 7. a kind of for the wear-resistant ceramic composite denitration catalyst of glass furnace and its preparation side according to claim 6
Method, it is characterised in that the wet base of catalyst, which is made, needs old more than 24h;Pre-filtering is stainless using specification 1 × 4mm's or 0.8 × 3mm
Steel filter screen.
It is 8. according to claim 6 a kind of for the wear-resistant ceramic composite denitration catalyst of glass furnace and its preparation side
Method, the extrusion pressure of vacuum-extruder described in its feature are 3 ~ 6MPa, 35 DEG C of extrusion temperature <, extrude vacuum -0.09MPa.
It is 9. according to claim 6 a kind of for the wear-resistant ceramic composite denitration catalyst of glass furnace and its preparation side
Method, it is characterised in that the solid-state adhesion agent is CMC, and the organic lubricant is stearic acid, and organic plasticising NMF is
PEO。
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