CN104415777A - Active powder preparation method - Google Patents
Active powder preparation method Download PDFInfo
- Publication number
- CN104415777A CN104415777A CN201310370475.5A CN201310370475A CN104415777A CN 104415777 A CN104415777 A CN 104415777A CN 201310370475 A CN201310370475 A CN 201310370475A CN 104415777 A CN104415777 A CN 104415777A
- Authority
- CN
- China
- Prior art keywords
- preparation
- active powder
- powder
- catalyst
- active
- 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
Abstract
The invention relates to an active powder preparation method, and belongs to the technical field of denitration catalysts. In the prior art, the existing denitration catalyst has the short service life and can not meet the denitration requirement under the low rotation speed of the ship diesel engine. With the active powder preparation method of the present invention, the problems in the prior art are solved. The active powder preparation method comprises: adding titanium dioxide powder to a first mixed solution prepared from ammonium metatungstate, deionized water and citric acid to obtain a first suspension, and sequentially carrying out drying and calcination to obtain titanium tungsten powder; and adding titanium dioxide powder to a second mixed solution prepared from ammonium metavanadate, deionized water and citric acid to obtain a second suspension, and sequentially carrying out drying and calcination to obtain titanium tungsten powder so as to obtain the active powder. According to the present invention, the primary modification and the secondary modification are performed on the active powder prepared through the method of the present invention, such that the active components are loaded in the matrix titanium dioxide powder in a step-by-step and layering manner so as to increase the denitration efficiency of the denitration catalyst prepared from the previous active powder under the low rotation speed of the ship diesel engine.
Description
Technical field
The invention belongs to denitrating catalyst technical field, be particularly applicable to the preparation method of the denitrating catalyst of diesel engine.
Background technology
Along with the deterioration of environmental quality, to the limit value also increasingly stringent of the moving source such as vehicle, boats and ships pollution emission, the nitrogen oxide (NO of one of environmental quality assessment index especially as a whole
x).There is research display, the NO discharged by boats and ships
xaccount for 14 ~ 15% of world's total release, specific region may be higher, and it not only can cause acid rain, photochemical fog etc. to destroy the series of problems of ball ecological environment, but also the health of human body in serious harm.Therefore, how effectively to remove nitrogen oxide and become the important topic that in current field of Environment Protection, attracts people's attention.Ammonia selective catalytic reduction (selectivecatalytic reduction, SCR) is due to ripe and efficient and become the denitration technology of main flow, and its key problem is just the development of catalyst and the adaptability of catalyst and various operating mode.Chinese scholars has carried out going deep into systematic research, as V to many catalyst systems
2o
5-WO
3/ TiO
2, MnO
2/ TiO
2, FeO
x/ TiO
2, CuO/TiO
2, Cr
2o
3/ TiO
2and CeO
2/ TiO
2deng.At present, the NH of industrial applications
3-SCR catalyst, mainly with TiO
2for carrier, then upload a certain amount of V
2o
5, WO
3, M
oo
3deng.For this reason, people are deepening constantly the research of denitration catalyst technology, to seek the wider denitrating catalyst of the scope of application, adapt to various operating mode with this, especially the low speed characteristics of boat diesel engine.
CN101480611B vanadium-doped titanium-base flue gas denitration catalyst material and preparation method thereof, a kind of vanadium-doped titanium-base flue gas denitration catalyst material of this disclosure of the invention and preparation method thereof, take surfactant as pore structure directed agents, adopt water solution system sol-gel process to prepare vanadium doping titanium base catalysis material, the doping of active component vanadium is with V
2o
5count 0.5 ~ 20wt%, adopt at sol-gel process situ doping mode of loading, not only preparation method is simple, production cost is low, and prepared denitration catalyst material specific area is larger, heat endurance is higher, there is higher denitration efficiency and wider active temperature windows, be applicable to coal-fired flue-gas removal of nitrogen oxide field.Adopt laboratory simulation flue gas evaluation display, when air speed is 10000h
-1nO content is under the condition of 1000ppm, and in the temperature range of 180 ~ 420 DEG C, the removal efficiency of NO reaches more than 95%, the defect of denitration catalyst agent material prepared by this employing impregnation method is that service life is short, and the nitrogen oxides treatment efficiency of catalyst when the diesel engine slow-speed of revolution is low.
CN101468314A Catalysts and its preparation method for low-temperature denitration of flue gas, this invention relates to a kind of Catalysts and its preparation method for low-temperature denitration of flue gas.It adopts SCR (SCR) technology, take vanadium oxide as active component, titanium oxide is carrier.And in this oxide catalyst, have part oxygen to replaced by fluorine, the method of Kaolinite Preparation of Catalyst, wherein active component vanadium oxide adopts infusion process load on carrier, carrier titanium oxide is prepared by sol-gel process, the time that fluorine replaces oxygen can be when preparing carrier titanium oxide, or during load active component vanadium oxide.Invention significantly improves the active and catalytic capability of low-temperature denitration, more than 200 DEG C can reach more than 90% NO removal efficiency, possess stronger industrial application value, the NH of nitrogen oxides in effluent can be widely used in
3sCR, the defect of denitration catalyst agent material prepared by this employing impregnation method is that service life is short, and the nitrogen oxides treatment efficiency of catalyst when the diesel engine slow-speed of revolution is low, can not adapt with various operating mode.
CN1101584992A urea scr catalyst and manufacture method thereof, this invention relates to a kind of selective reduction catalyst: wherein substantially along the longitudinal, and half catalyst (entrance) scribbles Mn/TiO
2, and second half catalyst (outlet) scribbles Fe-zeolite/ZSM, and prepare finishing coat by adding cerous carbonate, thus in finishing coat, form hole by the decomposition in roasting process, and increase the active surface sum effectiveness of performance of catalyst.The feature of this aspect is the preparation method of this selective reduction catalyst.The defect of denitration catalyst agent material prepared by this employing impregnation method is that service life is short, can not adapt with various operating mode.
CN101954281A is used for the cerium copper titanium compound oxide catalyst of denitrating flue gas and preparation method, and this disclosure of the invention a kind of cerium copper titanium compound oxide catalyst for denitrating flue gas and preparation method, the component of this catalyst comprises CeO
2, CuO and TiO
2.Catalyst preparing adopts coprecipitation, can reach desirable denitration effect.The advantage of this catalyst is: 1) have higher activity to the catalytic reduction of nitrogen oxides in effluent; 2) the adaptive temperature window of catalyst is wider, in 150 ~ 450 DEG C of whole temperature ranges, all have certain activity; 3) effectively can improve the runnability of catalyst under SO2 and H2O condition, to the bad working environments under sulfur dioxide and water etc. exist, there is stronger adaptability, exercisable wider; 4) raw materials is easy to get, preparation technology is simple, and catalyst cost is lower, and the defect of denitration catalyst agent material prepared by this employing coprecipitation is that service life is short, can not adapt with various operating mode.
CN101920213A take Metal-organic frame as low temperature SCR denitration catalyst of carrier and preparation method thereof, this invention design is a kind of with low temperature SCR denitration catalyst taking Metal-organic frame as carrier and preparation method thereof, belongs to air contaminant treatment technology and environment protection catalytic Material Field.Adopt infusion process in MOFs catalyst carrier, the oxide of one or more metallic elements of load Mn, Fe, Cu, V, Ce is active component, through super-dry, roasting with sieve, control to obtain institute's metal catalyst, with catalyst in gross mass for standard, reactive metal oxides load capacity is 1 ~ 10%, and the operating temperature of catalyst is 80 ~ 200 DEG C.Catalyst has larger specific area, higher low-temperature catalytic activity and denitration effect, there is wide prospects for commercial application in flue-gas denitration process, the defect that this method exists is that high-temperature catalytic activity is low, and application range of products is narrow, can not adapt with various operating mode.
The denitration technology of the main flow that SCR technology is administered as nitrogen oxide, especially be the denitrating catalyst of major matrix material with anatase titanium dioxide, be administer the most effective catalyst of nitrogen oxide, the denitrating catalyst of titanium dioxide matrix material has high denitration efficiency, preferably sulfur resistance, longer service life.But due to when considering that product uses, mechanism when the rear waste gas that the slow-speed of revolution of boat diesel engine causes and conventional denitrating catalyst haptoreaction changes to some extent, so conventional denitrating catalyst cannot meet the improvement of waste gas after boat diesel engine, during preparation technology requires, when extruding Faveolate denitration catalyst, common pug is expressed into 10 ~ 15 holes/cm
2hole density be unusual degree of difficulty, be the problem being difficult to overcome when extruder is shaping always.The present invention establishes a kind of boat diesel engine exhaust gas denitration method for preparing catalyst, in preparation process, a modification and twice-modified is carried out to titanium dioxide at denitrating catalyst, make active component substep, being carried in matrix titanium dioxide of layering, selective when adding reaction.With the addition of the Si oxide of plasticizer pyrophillite and aluminosilicate glass in pug simultaneously, add the plasticity of product and improve the mechanical strength of catalyst, especially the mechanical strength when stephanoporate thin wall is greatly improved, and improves the integrated level of catalyst when designing, 10 ~ 15 holes/cm
2loose structure add the surface area of integrated system, improve the denitration efficiency of boat diesel engine when the slow-speed of revolution.
It is short to there is service life in denitrating catalyst prepared by above prior art, can not adapt to various operating mode, and the denitration efficiency especially when the boat diesel engine slow-speed of revolution is low.
Summary of the invention
For solving existing titanium dioxide poor activity, the problem that the denitrating catalyst service life causing preparing with titanium dioxide is short, denitration efficiency is low, the invention provides a kind of is raw material with titanium dioxide, the preparation method of the active powder obtained after twice modification, and its technical scheme is as follows:
A preparation method for active powder, comprises following sequential steps:
Titanium dioxide is joined in the first mixed solution that ammonium metatungstate, deionized water and citric acid be mixed with, after the first suspension drying obtained, roasting, obtain titanium tungsten powder;
Again titanium dioxide is joined in the second mixed solution that ammonium metavanadate, deionized water and citric acid be mixed with, after the second suspension drying obtained, roasting, obtain titanium tungsten powder, obtain active powder.
Preferred version as the inventive method:
The mass ratio of described ammonium metatungstate and titanium dioxide is 5 ~ 10:90 ~ 95;
The mass ratio of described ammonium metavanadate and titanium tungsten powder is 0.1 ~ 1.5:98.5 ~ 99.9.
Further preferred version as the inventive method:
The compound method of described first mixed solution is as follows:
Using ammonium metatungstate as a modifier, join in deionized water, be mixed with ammonium metatungstate aqueous solution; Then using citric acid as hydrotropy dispersant, join in ammonium metatungstate aqueous solution, obtain the first mixed solution.
Further preferred version as the inventive method:
The compound method of described second mixed solution is as follows:
Using ammonium metavanadate as twice-modified dose, join in deionized water, be mixed with ammonium metavanadate aqueous solution; Then using citric acid as hydrotropy dispersant, join in ammonium metavanadate aqueous solution, obtain the second mixed solution.
Further preferred version as the inventive method:
The mass percent concentration of described ammonium metatungstate aqueous solution is 1 ~ 10%.
Further preferred version as the inventive method:
The mass percent concentration of described ammonium metavanadate aqueous solution is 0.1 ~ 0.5%.
Further preferred version as the inventive method:
In described first mixed solution, the addition of citric acid is 0.5 ~ 5% of ammonium metatungstate aqueous solution quality.
Further preferred version as the inventive method:
In described second mixed solution, the addition of citric acid is 0.1 ~ 0.5% of ammonium metavanadate aqueous solution quality.
Further preferred version as the inventive method:
The baking temperature of described first suspension is 60 ~ 120 DEG C, and drying time is 10 ~ 30h, and sintering temperature is 400 ~ 650 DEG C, and roasting time is 5 ~ 10h.
Further preferred version as the inventive method:
The baking temperature of described second suspension is 60 ~ 120 DEG C, and drying time is 10 ~ 30h, and the second suspension sintering temperature is after drying 400 ~ 600 DEG C, and roasting time is 5-10h.
The titanium dioxide used in the present invention is commercially available titanium dioxide, and specific area is more than or equal to 100m
2/ g, median 0.5 ~ 1.5 μm, crystallite dimension 5 ~ 15nm.
The active powder that the inventive method is prepared, through a modification and twice-modified, makes active component substep, being carried in matrix titanium dioxide of layering, improves the denitration efficiency of denitrating catalyst under the boat diesel engine slow-speed of revolution prepared with active powder.
With above-mentioned active powder for the method for boat diesel engine exhaust gas denitration catalyst prepared by raw material, comprise the following steps:
Step 1: dry powder is extruded in preparation:
Using pyrophillite as plasticizer, join in active powder, after Homogeneous phase mixing, obtain extruding dry powder, wherein the mass ratio of pyrophillite and active powder is 5 ~ 10:100;
Step 2: pug is extruded in preparation:
Dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and deionized water will be extruded and put into batch mixer, by the shear action of batch mixer, obtain active carbon pug;
The mass ratio wherein extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and deionized water is 50 ~ 80:3 ~ 30:0.5 ~ 5:3 ~ 10:0.5 ~ 5.0:0.5 ~ 5:10 ~ 30;
Wherein aluminium glue is Al
2o
30.5H
2o;
Step 3: prepare denitrating catalyst moulded pottery not yet put in a kiln to bake:
Active carbon pug is put into vacuum-extruder, through extruded, obtains Faveolate denitration catalyst moulded pottery not yet put in a kiln to bake;
Step 4: dry:
Faveolate denitration catalyst moulded pottery not yet put in a kiln to bake is put into steam drying stove, drying, obtain denitration catalyst blank;
Step 5: roasting:
Denitration catalyst blank is put into electric furnace, through roasting, obtains boat diesel engine exhaust gas denitration catalyst.
Preferably:
In described step 2, the mass ratio extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and deionized water is 60 ~ 70:4 ~ 30:0.5 ~ 4.0:4 ~ 10:0.5 ~ 4.0:0.5 ~ 5:20 ~ 30.
Preferably:
In described step 1, the mass percentage content of each component in pyrophillite is as follows:
Al
2o
3be 27.5 ~ 28.0%, SiO
2be 66.5 ~ 67.0%, FeO be 0.08 ~ 0.12%, Fe
2o
3be 0.18 ~ 0.22%, MgO be 0.18 ~ 0.23%, H
2o is 4 ~ 5%.
Preferably:
In described step 2, the median of aluminosilicate glass is 100 ~ 150 μm.
Preferably:
In described step 2, copper based molecular sieve adopts CuO to be carried in ZSM-5 molecular sieve, and wherein ZSM-5 molecular sieve duct bore is the load capacity of 0.2 ~ 1nm, CuO is 0.5 ~ 5.0% of the quality of ZSM-5 molecular sieve.
Preferably:
In described step 3, the vacuum of vacuum-extruder is 1.0 ~ 3.0MPa, and extrusion pressure is 1000 ~ 2000KN, and the hole density of Faveolate denitration catalyst base substrate is 10 ~ 15 holes/cm
2.
Preferably:
In described step 1, purity >=99.9% of calcium lignosulfonate, stearic purity >=99.9%;
In described step 2, the sectional dimension of Faveolate denitration catalyst moulded pottery not yet put in a kiln to bake is 150mm × 150mm, length 300 ~ 1200mm;
In described step 4, dry method be along the drying of direction, Faveolate denitration catalyst duct, and wherein baking temperature is 20 ~ 70 DEG C, drying time is 2 ~ 48h;
In described step 5, sintering temperature is 400 ~ 700 DEG C, and roasting time is 5 ~ 10h.
The mineral composition of the aluminium glue in the present invention is Al
2o
30.5H
2o.
The preparation method of the copper based molecular sieve in the present invention is as follows:
Configuration copper nitrate solution, wherein the mass concentration of copper nitrate is 0.2 ~ 10%, afterwards ZSM-5 molecular sieve is added in the aqueous solution of copper nitrate, wherein the mass ratio of ZSM-5 molecular sieve and copper nitrate aqueous solution is 40 ~ 60:50 ~ 70, dipping absorption 10 ~ 30h, carry out drying and roasting afterwards, wherein baking temperature is 20 ~ 100 DEG C, drying time is 2 ~ 36h; Sintering temperature is 400 ~ 600 DEG C, and roasting time is 5 ~ 10h.
The present invention establishes a kind of boat diesel engine exhaust gas denitration catalyst and preparation method, in denitrating catalyst preparation process, a modification and twice-modified is carried out to titanium dioxide, make active component substep, layering be carried in matrix titanium dioxide, improve the denitration efficiency of product under the boat diesel engine slow-speed of revolution, introduce plasticizer and aluminosilicate glass lamp Si oxide simultaneously, improve the plasticity of moulded pottery not yet put in a kiln to bake and the mechanical strength of product, improve the hole density when extrusion molding, reduce the wall thickness of product, improve denitrating catalyst short for service life, various operating mode is adapted to this, be particularly useful for the rear waste gas pollution control and treatment during boat diesel engine slow-speed of revolution, improve level of integrated system, reduce waste gas pollution control and treatment cost after boat diesel engine.Boat diesel engine exhaust gas denitration catalysis prepared by the present invention, under the diesel engine slow-speed of revolution, tail gas cleaning test shows, the clearance of NOx pernicious gas is all greater than 90%, and especially under the boat diesel engine slow-speed of revolution, engine speed still keeps NOx to have the transformation efficiency of 90% at 15 ~ 130r/min.
Specifically, present invention produces following technique effect:
1. this technique adopts a modification and twice-modified titanium dioxide as carrier, inserts in the solution of ammonium metatungstate by titanium dioxide, adopts citric acid as hydrotropy dispersant, enters drying and roasting obtains titanium tungsten powder after stirring; Carry out twice-modifiedly obtaining active powder to titanium tungsten powder with ammonium metavanadate again, titanium tungsten powder is inserted in the solution of ammonium metavanadate, drying and calcination activation is carried out after immersion, required active powder is obtained after activation terminates, make active component substep, being carried in matrix titanium dioxide of layering, selective when adding catalytic reaction; 2. adopt the pyrophillite of specific components as plastification material, improve the plasticity of pug, improve the mechanical strength of product; 3. adopt the aluminosilicate glass of specific components to be incorporated in powder as Si oxide, improve mechanical strength and the scour resistance of product; 4. carry out extrusion forming process to pug, obtaining hole density is 10 ~ 15 holes/cm
2porous honeycomb denitrating catalyst, increase the contact area of reaction bed of knowing clearly, the system that improve denitration reaction device squeezes integrated level; 5. product adopts copper base ZSM-5 molecular sieve as Supplementary active ingredients, improves the denitration efficiency of product under diesel engine slow-speed of revolution low temperature.Drying of the present invention and calcination activation obtain denitrating catalyst and still keep nitrogen oxide to have the transformation efficiency of 90% in engine speed at 15 ~ 130r/min, improve the level of integrated system of boat diesel engine denitration purifying device.
Accompanying drawing explanation
Preparation technology's flow chart of boats and ships denitrating catalyst that Fig. 1 is the active powder of the present invention and prepares with active powder.
Detailed description of the invention
Preparation technology's flow process of boats and ships denitrating catalyst as shown in Figure 1, mainly comprises: be that the ammonium metatungstate of 5% and the ammonium metavanadate of 0.41% carry out modification to titanium dioxide with quality, obtains active powder; Adopt pyrophillite to join in active powder as plasticizer to obtain extruding dry powder; Employing is extruded dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and appropriate deionized water and is prepared pug by the shear action of batch mixer; Adopt pug to add vacuum-extruder to carry out extrusion molding and obtain Faveolate denitration catalyst base substrate; Adopting Faveolate denitration catalyst base substrate to be placed in steam drying stove carries out dry along direction, Faveolate denitration catalyst duct; Dried product is inserted in electric furnace and carries out the steps such as calcination activation.
The active component V of catalyst
2o
5, WO
3mass ratio is 0.32%, 4.7% respectively.
The Supplementary active ingredients CuO mass ratio of catalyst is 0.45%.
The compound of a modification and twice-modified vanadium and tungsten, its presoma is respectively salts substances, and the present invention adopts meta-acid ammonium salt effect better.
High performance plasticizer, adopts pyrophillite, is 8% to mix according to mass percent.
High performance low alkali Si oxide, adopts aluminosilicate glass, is 10% to mix according to mass percent.
Extrude dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and the appropriate deionized water that obtain are prepared pug by the shear action of batch mixer, wherein extrude dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid, deionized water mass ratio be 50 ~ 80:3 ~ 30:0.5 ~ 5:3 ~ 10:0.5 ~ 5.0:0.5 ~ 5:10 ~ 30, the density of pug can be improved in the shear history of batch mixer.
Inserted by pug and carry out extruded in vacuum-extruder, hole density is 10 ~ 15 holes/cm
2, vacuum is 1.0 ~ 3.0MPa, and extrusion pressure is 1000 ~ 2000KN.
The pyrophillite mineral selected consist of Al
2o
3account for 27.8%, SiO
2account for 66.7%, FeO accounts for 0.1%, Fe
2o
3account for 0.2%, MgO accounts for 0.2%, H
2o accounts for 5.0%.The plasticity of the most favourable raising product of pyrophillite of this mineral composition.
The preparation method of boats and ships denitrating catalyst, adopt 5%(mass ratio) ammonium metatungstate as a modifier, adopt 0.4%(mass ratio) ammonium metavanadate as twice-modified dose, with extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid, deionized water prepare pug at the speed down cut of 50 ~ 200r/min, inserted by pug in vacuum-extruder extruded, hole density is 10 ~ 15 holes/cm
2vacuum is 1.0 ~ 3.0MPa, extrusion pressure is 1000 ~ 2000KN, obtain denitration catalyst blank, denitrating catalyst finished product is obtained after drying and calcination activation, Faveolate denitration catalyst base substrate is placed in steam drying stove, and carry out dry along direction, Faveolate denitration catalyst duct, baking temperature is 20 ~ 70 DEG C, drying time is 2 ~ 48h.Inserted by product in electric furnace and carry out calcination activation, sintering temperature is 400 ~ 700 DEG C, and roasting time is 5-10h.The catalyst that the method is prepared is compared with traditional catalyst, there is higher plasticity and the mechanical strength of product, improve the hole density when extrusion molding, reduce the wall thickness of product, improve denitrating catalyst short for service life, adapt to various operating mode with this, be particularly useful for the rear waste gas pollution control and treatment during boat diesel engine slow-speed of revolution, improve level of integrated system.
According to certain marine diesel engine, engine conditions is: four-stroke-cycle, water-cooled, in-line arrangement, charge inter cooling, directly injection, high-pressure common rail, discharge capacity is 244.5L, respectively under the slow-speed of revolution, medium speed, high rotating speed, carry out clean-up effect detection to denitrating catalyst product obtained as stated above, the nitrogen oxide after purification all meets the emission limit in " International Maritime Organization IMO TierIII regulation ".
The inventive method is utilized to obtain exemplary embodiments: a kind of boat diesel engine exhaust gas denitration catalyst obtained according to the method described above, the denitrating catalyst product size prepared is 150mm × 150mm × 300mm, catalyst endoporus aperture 2.2mm, inwall wall thickness is 0.4mm, outer wall wall thickness is 0.6mm, pitch 2.6mm.Active component contained by denitrating catalyst is V
2o
5, WO
3mass ratio is 0.32%, 4.7% respectively.The Supplementary active ingredients CuO mass ratio of catalyst is 0.45%, and the density of product is 450g/l, and in denitrating system, catalyst is divided into 3 layers, and in every layer, catalyst is arranged as 3 × 4 pieces, 12 pieces every layer, 36 pieces altogether.Under each rotating speed to this consumption ratio of nitrogen oxide removal efficiency, ammonia in table 2 and table 3.
Emission limit in table 1 " International Maritime Organization IMO Tier III regulation "
The clearance of nitrogen oxide under each rotating speed of table 2
This consumption ratio of reducing agent ammonia under the typical rotating speed of table 3
Embodiment 1:
Prepare active powder:
Steps A a: modification, prepare titanium tungsten powder, comprise following sequential steps:
Get ammonium metatungstate and titanium dioxide that mass ratio is 8:92;
Using ammonium metatungstate as a modifier, join in deionized water, be mixed with the ammonium metatungstate solution that mass percent concentration is 5%;
Using citric acid as hydrotropy dispersant, join in ammonium metatungstate solution, wherein the addition of citric acid is 1% of ammonium metatungstate aqueous solution quality, obtains mixed solution;
Joined by titanium dioxide in mixed solution, after stirring, be mixed with the first suspension, wherein mixing speed is 100r/min;
Then by after the first suspension drying, roasting, obtain titanium tungsten powder, wherein baking temperature is 90 DEG C, and drying time is 15h, and sintering temperature is 600 DEG C, and roasting time is 16h;
Step B: twice-modified, prepares target product, comprises following sequential steps:
Get ammonium metavanadate as twice-modified dose, join in deionized water, be mixed with the ammonium metavanadate solution that mass percent concentration is 0.4%, wherein the mass ratio of ammonium metavanadate and titanium tungsten powder is 0.9:99.1;
Using citric acid as hydrotropy dispersant, join in ammonium metavanadate solution, wherein the addition of citric acid is 0.4% of ammonium metavanadate aqueous solution quality, obtains mixed solution;
Join in mixed solution by titanium tungsten powder, after stirring, be mixed with the second suspension, wherein mixing speed is 100r/min;
Then by after the second suspension drying, roasting, obtain active powder, wherein baking temperature is 90 DEG C, and drying time is 12h, and sintering temperature is 550 DEG C, and roasting time is 10h.
Described titanium dioxide is commercially available titanium dioxide, specific area 120m
2/ g, median 1.0 μm, crystallite dimension 10nm.
Boats and ships denitrating catalyst and preparation method, comprise following sequential steps:
Step 1: dry powder is extruded in preparation:
Using pyrophillite as plasticizer, join in active powder, after Homogeneous phase mixing, obtain extruding dry powder, wherein the mass ratio of pyrophillite and active powder is 8:92.
Step 2: pug is extruded in preparation:
Pug is prepared by the shear action of batch mixer by extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and appropriate deionized water.
The described mass ratio extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and appropriate deionized water is 75:10:2:9:2:2:30.
The median of described sial glass requires 120.
Described plasticizer is pyrophillite, and its addition (mass ratio) is 8%.
The mineral composition of described pyrophillite: Al
2o
3account for 27.8%, SiO
2account for 66.7%, FeO accounts for 0.1%, Fe
2o
3account for 0.2%, MgO accounts for 0.2%, H
2o accounts for 5.0%.
Described calcium lignosulfonate, stearic purity requirement >=99.9%.
Described copper based molecular sieve adopts CuO to be carried in ZSM-5 molecular sieve, and the load capacity of CuO is 5.0%.
Step 3: prepare denitrating catalyst moulded pottery not yet put in a kiln to bake:
Active carbon pug is added vacuum-extruder to carry out extruded, and hole density is 15/cm
2; , vacuum is 2.0MPa, and extrusion pressure is 1500KN, and the sectional dimension of moulded pottery not yet put in a kiln to bake is 150mm × 150mm, length 300mm.
Step 4: dry moulded pottery not yet put in a kiln to bake:
Faveolate denitration catalyst base substrate is placed in steam drying stove, and carry out along direction, Faveolate denitration catalyst duct dry, baking temperature is 60 DEG C, drying time 16h.
Step 5: roasting moulded pottery not yet put in a kiln to bake:
Inserted by product in electric furnace and carry out calcination activation, sintering temperature is 620 DEG C, roasting time 10h.
Embodiment 2:
Prepare active powder:
Steps A a: modification, prepare titanium tungsten powder, comprise following sequential steps:
Get ammonium metatungstate and titanium dioxide that mass ratio is 10:90;
Using ammonium metatungstate as a modifier, join in deionized water, be mixed with the ammonium metatungstate solution that mass percent concentration is 3%;
Using citric acid as hydrotropy dispersant, join in ammonium metatungstate solution, wherein the addition of citric acid is 0.6% of ammonium metatungstate aqueous solution quality, obtains mixed solution;
Joined by titanium dioxide in mixed solution, after stirring, be mixed with the first suspension, wherein mixing speed is 70r/min;
Then by after the first suspension drying, roasting, obtain titanium tungsten powder, wherein baking temperature is 80 DEG C, and drying time is 13h, and sintering temperature is 580 DEG C, and roasting time is 14h;
Step B: twice-modified, prepares target product, comprises following sequential steps:
Get ammonium metavanadate as twice-modified dose, join in deionized water, be mixed with the ammonium metavanadate solution that mass percent concentration is 0.2%, wherein the mass ratio of ammonium metavanadate and titanium tungsten powder is 1.2:98.8;
Using citric acid as hydrotropy dispersant, join in ammonium metavanadate solution, wherein the addition of citric acid is 0.2% of ammonium metavanadate aqueous solution quality, obtains mixed solution;
Join in mixed solution by titanium tungsten powder, after stirring, be mixed with the second suspension, wherein mixing speed is 70r/min;
Then by after the second suspension drying, roasting, obtain active powder, wherein baking temperature is 80 DEG C, dry 10h, and sintering temperature is 525 DEG C, and roasting time is 6h.
Described titanium dioxide is commercially available titanium dioxide, specific area 100m
2/ g, median 0.6 μm, crystallite dimension 8nm.
Boats and ships denitrating catalyst and preparation method, comprise following sequential steps:
Step 1: dry powder is extruded in preparation:
Using pyrophillite as plasticizer, join in active powder, after Homogeneous phase mixing, obtain extruding dry powder, wherein the mass ratio of pyrophillite and active powder is 5:95;
Step 2: pug is extruded in preparation:
Pug is prepared by the shear action of batch mixer by extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and appropriate deionized water.
The described mass ratio extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and appropriate deionized water is 78:9:1.5:7:1.7:1.7:30.
The median of described sial glass requires at 100 μm.
Described plasticizer is pyrophillite, and its addition (mass ratio) is 5%.
The mineral composition of described pyrophillite: Al
2o
3account for 27.8%, SiO
2account for 66.7%, FeO accounts for 0.1%, Fe
2o
3account for 0.2%, MgO accounts for 0.2%, H
2o accounts for 5.0%.
Described calcium lignosulfonate, stearic purity requirement >=99.9%.
Described copper based molecular sieve adopts CuO to be carried in ZSM-5 molecular sieve, and the load capacity of CuO is 2.0%.
Step 3: prepare denitrating catalyst moulded pottery not yet put in a kiln to bake:
Active carbon pug is added vacuum-extruder to carry out extruded, and hole density is 10 holes/cm
2; , vacuum is 1.5MPa, and extrusion pressure is 1000KN, and the sectional dimension of moulded pottery not yet put in a kiln to bake is 150mm × 150mm, length 300mm.
Step 4: dry moulded pottery not yet put in a kiln to bake:
Faveolate denitration catalyst base substrate is placed in steam drying stove, carries out along direction, Faveolate denitration catalyst duct dry, baking temperature is 50 DEG C, drying time 12h.
Step 5: roasting moulded pottery not yet put in a kiln to bake:
Inserted by product in electric furnace and carry out calcination activation, sintering temperature is 580 DEG C, roasting time 8h.
Embodiment 3:
Prepare active powder:
Steps A a: modification, prepare titanium tungsten powder, comprise following sequential steps:
Get ammonium metatungstate and titanium dioxide that mass ratio is 6:94;
Using ammonium metatungstate as a modifier, join in deionized water, be mixed with the ammonium metatungstate solution that mass percent concentration is 10%;
Using citric acid as hydrotropy dispersant, join in ammonium metatungstate solution, wherein the addition of citric acid is 3% of ammonium metatungstate aqueous solution quality, obtains mixed solution;
Joined by titanium dioxide in mixed solution, after stirring, be mixed with the first suspension, wherein mixing speed is 200r/min;
Then by after the first suspension drying, roasting, obtain titanium tungsten powder, wherein baking temperature is 120 DEG C, and drying time is 30h, and sintering temperature is 650 DEG C, and roasting time is 20h;
Step B: twice-modified, prepares target product, comprises following sequential steps:
Get ammonium metavanadate as twice-modified dose, join in deionized water, be mixed with the ammonium metavanadate solution that mass percent concentration is 0.5%, wherein the mass ratio of ammonium metavanadate and titanium tungsten powder is 0.7:92.3;
Using citric acid as hydrotropy dispersant, join in ammonium metavanadate solution, wherein the addition of citric acid is 0.5% of ammonium metavanadate aqueous solution quality, obtains mixed solution;
Join in mixed solution by titanium tungsten powder, after stirring, be mixed with the second suspension, wherein mixing speed is 200r/min;
Then by after the second suspension drying, roasting, obtain active powder, wherein baking temperature is 120 DEG C, and drying time is 20h, and sintering temperature is 630 DEG C, and roasting time is 20h.
Described titanium dioxide is commercially available titanium dioxide, specific area 160m
2/ g, median 1.5 μm, crystallite dimension 15nm.
Boats and ships denitrating catalyst and preparation method, comprise following sequential steps:
Step 1: dry powder is extruded in preparation:
Using pyrophillite as plasticizer, join in active powder, after Homogeneous phase mixing, obtain extruding dry powder, wherein the mass ratio of pyrophillite and active powder is 10:90;
Step 2: pug is extruded in preparation:
Pug is prepared by the shear action of batch mixer by extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and appropriate deionized water.
The described mass ratio extruding dry powder, aluminosilicate glass, aluminium glue, copper based molecular sieve, calcium lignosulfonate, stearic acid and appropriate deionized water is 72:20:3:10:3:3:30.
The median of described sial glass requires at 150 μm.
Described plasticizer is pyrophillite, and its addition (mass ratio) is 10%.
The mineral composition of described pyrophillite: Al
2o
3account for 27.8%, SiO
2account for 66.7%, FeO accounts for 0.1%, Fe
2o
3account for 0.2%, MgO accounts for 0.2%, H
2o accounts for 5.0%.
Described calcium lignosulfonate, stearic purity requirement >=99.9%.
Described copper based molecular sieve adopts CuO to be carried in ZSM-5 molecular sieve, and the load capacity of CuO is 4.5%.
Step 3: prepare denitrating catalyst moulded pottery not yet put in a kiln to bake:
Active carbon pug is added vacuum-extruder to carry out extruded, and hole density is 14 holes/cm
2; , vacuum is 3.0MPa, and extrusion pressure is 1900KN, and the sectional dimension of moulded pottery not yet put in a kiln to bake is 150mm × 150mm, length 300mm.
Step 4: dry moulded pottery not yet put in a kiln to bake:
Faveolate denitration catalyst base substrate is placed in steam drying stove, and carry out along direction, Faveolate denitration catalyst duct dry, baking temperature is 70 DEG C, drying time 30h.
Step 5: roasting moulded pottery not yet put in a kiln to bake:
Inserted by product in electric furnace and carry out calcination activation, sintering temperature is 700 DEG C, roasting time 20h.
Claims (10)
1. a preparation method for active powder, is characterized in that comprising following sequential steps:
Titanium dioxide is joined in the first mixed solution that ammonium metatungstate, deionized water and citric acid be mixed with, after the first suspension drying obtained, roasting, obtain titanium tungsten powder;
Again titanium dioxide is joined in the second mixed solution that ammonium metavanadate, deionized water and citric acid be mixed with, after the second suspension drying obtained, roasting, obtain titanium tungsten powder, obtain active powder.
2. the preparation method of a kind of active powder according to claim 1, is characterized in that:
The mass ratio of described ammonium metatungstate and titanium dioxide is 5 ~ 10:90 ~ 95;
The mass ratio of described ammonium metavanadate and titanium tungsten powder is 0.1 ~ 1.5:98.5 ~ 99.9.
3. the preparation method of a kind of active powder according to claim 1 and 2, is characterized in that:
The compound method of described first mixed solution is as follows:
Using ammonium metatungstate as a modifier, join in deionized water, be mixed with ammonium metatungstate aqueous solution; Then using citric acid as hydrotropy dispersant, join in ammonium metatungstate aqueous solution, obtain the first mixed solution.
4. the preparation method of a kind of active powder according to claim 3, is characterized in that:
The compound method of described second mixed solution is as follows:
Using ammonium metavanadate as twice-modified dose, join in deionized water, be mixed with ammonium metavanadate aqueous solution; Then using citric acid as hydrotropy dispersant, join in ammonium metavanadate aqueous solution, obtain the second mixed solution.
5. the preparation method of a kind of active powder according to claim 4, is characterized in that:
The mass percent concentration of described ammonium metatungstate aqueous solution is 1 ~ 10%.
6. the preparation method of a kind of active powder according to claim 4, is characterized in that:
The mass percent concentration of described ammonium metavanadate aqueous solution is 0.1 ~ 0.5%.
7. the preparation method of a kind of active powder according to claim 6, is characterized in that:
In described first mixed solution, the addition of citric acid is 0.5 ~ 5% of ammonium metatungstate aqueous solution quality.
8. the preparation method of a kind of active powder according to claim 7, is characterized in that:
In described second mixed solution, the addition of citric acid is 0.1 ~ 0.5% of ammonium metavanadate aqueous solution quality.
9. the preparation method of a kind of active powder according to claim 8, is characterized in that:
The baking temperature of described first suspension is 60 ~ 120 DEG C, and drying time is 10 ~ 30h, and sintering temperature is 400 ~ 650 DEG C, and roasting time is 5 ~ 10h.
10. the preparation method of a kind of active powder according to claim 9, is characterized in that:
The baking temperature of described second suspension is 60 ~ 120 DEG C, and drying time is 10 ~ 30h, and the second suspension sintering temperature is after drying 400 ~ 600 DEG C, and roasting time is 5-10h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310370475.5A CN104415777A (en) | 2013-08-22 | 2013-08-22 | Active powder preparation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310370475.5A CN104415777A (en) | 2013-08-22 | 2013-08-22 | Active powder preparation method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104415777A true CN104415777A (en) | 2015-03-18 |
Family
ID=52966555
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310370475.5A Pending CN104415777A (en) | 2013-08-22 | 2013-08-22 | Active powder preparation method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104415777A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106111121A (en) * | 2016-06-16 | 2016-11-16 | 上海净球环保科技有限公司 | A kind of preparation method of titanio activity powder |
| CN106268773A (en) * | 2016-06-29 | 2017-01-04 | 浙江浙能催化剂技术有限公司 | A kind of thin-walled wide active temperature windows denitrating catalyst and preparation method thereof |
| CN107980772A (en) * | 2017-11-07 | 2018-05-04 | 常州布奇纺织有限公司 | A kind of preparation method of bacteriostatic and odour removing permanent seal cooling eliminating smell agent |
| CN112403485A (en) * | 2020-11-19 | 2021-02-26 | 高化学（江苏）化工新材料有限责任公司 | V/Cu/B/W-TiO2-ZrO2Production method of composite low-temperature denitration catalyst |
| CN115624968A (en) * | 2022-11-14 | 2023-01-20 | 国能龙源环保有限公司 | Method for preparing denitration catalyst by utilizing waste wind power blades and application |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101502796A (en) * | 2009-03-20 | 2009-08-12 | 无锡市宜刚耐火材料有限公司 | Integral honeycomb selective catalytic reduction catalyst for flue gas denitration and method for preparing the same |
| CN102000562A (en) * | 2010-12-29 | 2011-04-06 | 中国科学院广州能源研究所 | High-efficiency denitration catalyst and preparation method thereof |
| CN102416321A (en) * | 2011-11-30 | 2012-04-18 | 广州市威格林环保科技有限公司 | Preparation method of SCR (Selective Catalytic Reduction) vanadium-series catalyst used in denitration of tail gas of diesel vehicle |
| CN102921403A (en) * | 2012-09-11 | 2013-02-13 | 河南佰利联化学股份有限公司 | Method for preparing V2O5-WO3/TiO2 powder for making denitration catalyst |
| CN102935387A (en) * | 2012-11-05 | 2013-02-20 | 北京华电光大新能源环保技术有限公司 | Continuous production device and production process of selective catalytic reduction (SCR) plate-type denitration catalyst |
-
2013
- 2013-08-22 CN CN201310370475.5A patent/CN104415777A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101502796A (en) * | 2009-03-20 | 2009-08-12 | 无锡市宜刚耐火材料有限公司 | Integral honeycomb selective catalytic reduction catalyst for flue gas denitration and method for preparing the same |
| CN102000562A (en) * | 2010-12-29 | 2011-04-06 | 中国科学院广州能源研究所 | High-efficiency denitration catalyst and preparation method thereof |
| CN102416321A (en) * | 2011-11-30 | 2012-04-18 | 广州市威格林环保科技有限公司 | Preparation method of SCR (Selective Catalytic Reduction) vanadium-series catalyst used in denitration of tail gas of diesel vehicle |
| CN102921403A (en) * | 2012-09-11 | 2013-02-13 | 河南佰利联化学股份有限公司 | Method for preparing V2O5-WO3/TiO2 powder for making denitration catalyst |
| CN102935387A (en) * | 2012-11-05 | 2013-02-20 | 北京华电光大新能源环保技术有限公司 | Continuous production device and production process of selective catalytic reduction (SCR) plate-type denitration catalyst |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106111121A (en) * | 2016-06-16 | 2016-11-16 | 上海净球环保科技有限公司 | A kind of preparation method of titanio activity powder |
| CN106268773A (en) * | 2016-06-29 | 2017-01-04 | 浙江浙能催化剂技术有限公司 | A kind of thin-walled wide active temperature windows denitrating catalyst and preparation method thereof |
| CN107980772A (en) * | 2017-11-07 | 2018-05-04 | 常州布奇纺织有限公司 | A kind of preparation method of bacteriostatic and odour removing permanent seal cooling eliminating smell agent |
| CN112403485A (en) * | 2020-11-19 | 2021-02-26 | 高化学（江苏）化工新材料有限责任公司 | V/Cu/B/W-TiO2-ZrO2Production method of composite low-temperature denitration catalyst |
| CN115624968A (en) * | 2022-11-14 | 2023-01-20 | 国能龙源环保有限公司 | Method for preparing denitration catalyst by utilizing waste wind power blades and application |
| CN115624968B (en) * | 2022-11-14 | 2024-02-02 | 国能龙源环保有限公司 | Method for preparing denitration catalyst by using waste wind power blades and application |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104415781A (en) | Ship diesel engine gas exhaust denitration catalyst preparation method | |
| CN109225248B (en) | Honeycomb type low-temperature denitration catalyst and preparation process thereof | |
| CN102861595B (en) | Honeycombed SCR (selective catalytic reduction) denitrification catalyst for low-temperature flue gas denitrification and preparation method thereof | |
| CN106807356B (en) | A kind of low temperature SCR denitration catalyst and its methods for making and using same | |
| CN103464194A (en) | SCR (Selective catalytic reduction) monolithic honeycombed catalyst for low-temperature flue gas de-nitrification and preparation method thereof | |
| CN101428212B (en) | Selective catalysis reduction denitrate catalyst for composite carrier flue gas and preparation method thereof | |
| CN104415777A (en) | Active powder preparation method | |
| CN105107514A (en) | Honeycomb non-vanadium denitration shaping catalyst, preparation method and application thereof | |
| CN103769083B (en) | A kind of NO_x Reduction by Effective composite oxide catalysts and its preparation method and application | |
| CN104162421A (en) | Preparation method of high temperature resistant vanadium tungsten titanium oxide catalyst | |
| CN104415755A (en) | Denitration catalyst adopting modified active carbon as matrix material, and preparation method thereof | |
| CN107362822B (en) | Preparation method of integral molecular sieve SCR catalytic reactor | |
| CN109433254A (en) | A kind of confinement molecular sieve denitrating catalyst and preparation method thereof | |
| CN106140150A (en) | A kind of honeycomb fashion cerium zirconium manganese titanio denitrating catalyst and preparation method thereof | |
| CN101703927A (en) | Preparation process of nano catalyst honeycomb | |
| CN103861581A (en) | Perovskite-type substance La<1-x>Sr<x>CrO<3>, heat-engine plant denitration composite catalyst, and preparation methods of perovskite-type substance La<1-x>Sr<x>CrO<3> and heat-engine plant denitration composite catalyst | |
| CN106582874A (en) | High temperature resistant phosphotungstic acid adsorbed iron-based oxide catalyst and preparation method thereof | |
| CN104998684B (en) | A kind of rare earth modified SCR denitration and preparation method thereof | |
| CN109967069A (en) | A kind of low-temperature SCR catalyst and preparation method thereof for cement kiln flue gas denitration | |
| CN112403485A (en) | V/Cu/B/W-TiO2-ZrO2Production method of composite low-temperature denitration catalyst | |
| CN106111124A (en) | A kind of denitrating catalyst with modified activated carbon as matrix material and preparation method thereof | |
| CN114260015A (en) | Flue gas denitration molded catalyst and preparation method and application thereof | |
| CN104415766B (en) | Coal-fired power station flue gas denitration composite catalyst and preparation method thereof | |
| CN104415763B (en) | Modified diatomite and preparation method thereof | |
| CN105688932B (en) | A kind of derv fuel tail gas NOx, CO, HC cleaning catalyst and preparation method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150318 |
|
| RJ01 | Rejection of invention patent application after publication |