CN105367114A - Exhaust purifier and preparation method thereof - Google Patents
Exhaust purifier and preparation method thereof Download PDFInfo
- Publication number
- CN105367114A CN105367114A CN201510799273.1A CN201510799273A CN105367114A CN 105367114 A CN105367114 A CN 105367114A CN 201510799273 A CN201510799273 A CN 201510799273A CN 105367114 A CN105367114 A CN 105367114A
- Authority
- CN
- China
- Prior art keywords
- exhaust purifier
- carrier
- honeycomb ceramic
- mixed
- rare earth
- 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
Landscapes
- Catalysts (AREA)
- Compositions Of Oxide Ceramics (AREA)
Abstract
The present invention discloses an exhaust purifier and a preparation method thereof, the exhaust purifier includes a housing and a ceramic honeycomb carrier, the ceramic honeycomb carrier is disposed within the housing, the porous structure of the ceramic honeycomb carrier includes a curved snake shaped channel and a straight channel, the straight channel is communicated with the curved snake shaped channel, and the ceramic honeycomb carrier includes the following components by mass: 6-10% of a sintering additive, 2-5% of mixed clay, 2-5% of a rare earth oxide, 1-2% of reinforced fiber and the balance of alumina powder. Through refining of the alumina particle size and addition of the mixed clay, the reinforced fiber and the rare earth oxide, the carrier has high compressive strength, lower thermal expansion coefficient and low sintering temperature, and the preparation method is simple and efficient and suitable for exhaust purifier scale production.
Description
Technical field
The present invention relates to purifying vehicle exhaust gas field, especially a kind of exhaust purifier and preparation method thereof.
Background technology
Along with becoming increasingly conspicuous of air pollution problems inherent and increasing sharply of automobile quantity, waste gas one of primary pollution source becoming urban air pollution of motor vehicle emission.Objectionable impurities in vehicle exhaust mainly contains CO, NOx and HC, polycyclic aromatic hydrocarbons (PAH) and suspended substance (SPM) etc.NOx and HC, in an atmosphere through a series of photochemical reaction, easily generates the very strong material of the multiple oxidisability such as ozone, forms photo-chemical smog.The health of photo-chemical smog not only serious harm people, and can do great damage to animals and plants and various material.
Exhaust purifier, is mounted in most important outer purifier in automobile exhaust system, and the obnoxious flavoures such as CO, HC and NOx that vehicle exhaust can be discharged by it change harmless carbonic acid gas, water and nitrogen into by oxidation and reductive action.When the vehicle exhaust of high temperature is by refining plant, scavenging agent in exhaust purifier will strengthen the activity of CO, HC and NOx tri-kinds of gases, impel it to carry out certain oxidation-reduction chemical reaction, wherein CO is at high temperature oxidized into colourless, nontoxic carbon dioxide; HC compound is at high temperature oxidized to water (H
20) and carbonic acid gas; NOx is reduced into nitrogen and oxygen.Three kinds of obnoxious flavoures become innocuous gas, and vehicle exhaust is purified.
Exhaust purifier comprises housing, carrier and is covered in the catalyzer of carrier surface.Early stage carrier many employings particulate vector, but due to the catalyzer of particulate vector have that packing density is large, bed resistance large, the easy shortcoming such as pulverizing, be unsuitable for purifying vehicle exhaust.And the passage of cellular monolithic catalytic agent carrier owing to having longitudinally, continuously, not stopped, the advantages such as resistance of exhaust is little, are widely used in the purification of vehicle exhaust, this kind of carrier of the many employings of current auto-exhaust catalyst in research afterwards.Early 1970s, 3M company and Ford's sintering process produce a kind of honeycomb ceramic carrier, within 1972, Corning Incorporated also develops a kind of honeycomb ceramic carrier, within 1986, Corning Incorporated produces honeycomb ceramic carrier at West Germany's instrument factory, to meet the needs of European car industry, the large-scale promotion for automotive catalyst has established solid basic substance.China greatly about 20th century the mid-80 start to produce honeycomb ceramic carrier, although have passed through the development of more than ten years, due to the reason such as technology, equipment, compared with external product, also have a certain distance.
Ceramic monolith is now widely used catalyst carrier for purifying vehicle tail gas, wherein more commonly CORDIERITE HONEYCOMB CERAMIC CARRIER.Industrialized cordierite ceramic preparation method is raw material mainly with kaolin, talcum or pure component oxide compound, adopts high temperature solid state reaction synthesis.It is simple that the method has production technique, production efficiency advantages of higher; But its greatest problem existed is exactly that synthesis temperature is high, and energy consumption is large, and sintering temperature reaches 1390 ~ 1400 DEG C, and its sintering warm area is very narrow.As introduced glassy phase, suitably can reduce the sintering temperature of cordierite ceramic, widening its sintering warm area, but improve its thermal expansivity, reducing the ability of anti-thermal shock and erosion.Precipition wrapping method and sol-gel method craft require relatively stricter, and building-up process is complicated, and raw material mostly is organic compound, expensive, and some is also harmful, is difficult to meet industrial application requirement.
Add auxiliary agent in utilization and improve cordierite ceramic aspect of performance, auxiliary agent mostly is single constituent element, often mean thermal expansion coefficients is very little, but there is larger difference in the thermal expansivity of its a axle and c-axis, be difficult to " zero thermal expansion " and Anisotropically heat effects are coordinated mutually, thus reduce the thermal characteristics of cordierite ceramic.
Aluminum oxide is also a kind of common stupalith, there is many excellent performances such as high temperature resistant, wear-resisting, corrosion-resistant, anti-oxidant, but because aluminum oxide self cationic charge is many, the features such as radius is little, and ionic linkage is strong, cause its lattice energy larger, spread coefficient is lower, sintering temperature is high, also receives certain restriction because the defect that its fragility is large, thermal expansivity is high makes it apply in addition, therefore needs a kind of effective ways that can solve the problem of searching badly.
Summary of the invention
For solving the problem, the invention discloses a kind of exhaust purifier and preparation method thereof, the carrier of this purification agent for treating waste gas take aluminum oxide as matrix, adds the carrier that sintering aid, mixed clay, rare earth oxide and strongthener make to obtain and have high compressive strength, lower thermal expansivity and lower sintering temperature.
Technical scheme of the present invention is: a kind of exhaust purifier, comprise housing and honeycomb ceramic carrier, honeycomb ceramic carrier is fixed in housing, the vesicular structure of described honeycomb ceramic carrier comprises bending serpentine channel and straight way, and straight way is communicated on serpentine channel, and component and the massfraction thereof of described honeycomb ceramic carrier comprise: sintering aid: 6-10%, mixed clay: 2-5%, rare earth oxide: 2-5%, fortifying fibre: 1-2%, surplus is alumina powder jointed.(wherein straight way is communicated to carrier surface, serpentine channel is arranged on carrier inside, the intake resistance that can reduce carrier surface is so set, thus improve high-speed and high-temperature tail gas and enter the efficiency that carrier carries out purifying) bonding between ceramic particle be that outer to increase temperature the glassy phase that binding agent formed under firing temperature bonding, mixed clay forms one deck glassy phase in sintering process on the surface of blapharoplast, and assemble at the point of contact place of two particles, form neck, the intensity of stupalith is improved.Act on when the add-on of mixed clay is less than 2% in the present invention that not obvious (in stupalith, the ligation of dystectic composition is abundant not, very easily form faint gap in carrier inside simultaneously, thus in pottery inner formation defect), and when being greater than 5%, the intensity of pottery does not only increase and sharply reduces on the contrary.This is because in the preparation process of slurry, along with the increase of mixed clay add-on, the viscosity of slurry constantly increases, and when the viscosity of slurry reaches more than 1000mPas, pottery produces streamlined crackle when burning till, the intensity of goods is reduced greatly.
Preferred as one, the aperture ratio of straight way and serpentine channel is 4:(4-5).At the serpentine channel that the inner setting unit of ceramic monolith is bending, and be communicated with straight way, make exhaust gas flow, through connectivity part formation eddy current or turbulent flow, irregular mixing occur, play the effect of stirring, serpentine channel too increases contact area and the contact pressure of tail gas and channel surface catalyzer simultaneously, effectively improves catalytic efficiency.Straight way and serpentine channel are when having the aperture of formed objects, the intake pressure of serpentine channel is higher than straight way, the aperture ratio slightly reducing straight way and serpentine channel can make ceramic monolith inner because of stressed more even, and its aperture ratio controls as 4:(4-5) ceramic monolith can be avoided to crack.
Preferred as one, described straight way is (5-6) with the pore volume ratio of serpentine channel: (4-5).When the pore volume ratio of straight way and serpentine channel is (5-6): time (4-5), control straight way volume and be more than or equal to serpentine channel volume, the intake resistance of tail gas is not too large, also can not exceed cracking limit with the contact pressure of hole wall, be conducive to carrying out smoothly of tail gas clean-up.
Preferred as one, alumina powder jointed particle diameter is 150-200nm.Common aluminum oxide ceramics often needs higher sintering temperature and adds its application cost in exhaust purifier.Because sintering is the migration being realized material by surface tension, therefore need higher activation energy, and the alumina ceramic grain particle diameter of refinement is little, specific surface area is large, surfactivity is high, the distance of interparticle diffusion is short, only need lower sintering activating energy and sintering temperature, obviously can improve the physicals of ceramic body, demonstrate excellent mechanical property.
Preferred as one, sintering aid is MgO, CaO, SiO
2, V
2o
5, Fe
2o
3, TiO
2in at least two kinds.Multiple sintering aid add thermal expansivity and the sintering temperature that effectively can reduce alumina ceramic material, improve sintering character, because the surface energy of nanometer alumina powder particle is larger, in the process of high temperature sintering densification, the easy ramp of crystal grain affects material mechanical performance, and in alumina-ceramic coating, add sintering aid, its crystal grain can be suppressed to grow up when high temperature on the one hand, on the other hand, also can reduce its sintering temperature.
Preferred as one, mixed clay is pretreated through 1400 DEG C of high temperature.After pretreated, mixed clay is ground, be ground to its granularity and be less than 0.2 μm.High Temperature Pre process can remove crystal water more in mixed clay, volatile matter and impurity, particle is made to be easy to grinding distribution, be conducive to being formed with blapharoplast evenly mix, putting forward high-quality stability, fine and closely woven micropore can also be formed in mixed clay simultaneously, forming miniature heat transfer path when sintering, improve the efficient of the microvoid structure of ceramic monolith, passage has higher activity simultaneously, thus improves sintering quality, and prevents from damaged distortion occurs because being heated inequality.The pretreated time must be controlled well, and because pretreated temperature is higher, the time can be effective more than 5min, but can not more than 10min, otherwise clay can start porcelain, therefore pretreatment time is 5-10min.Mixed clay uses as high-temperature agglomerant in the present invention, and the fineness of ceramic matrix grain diameter and high-temperature agglomerant controls extremely important.Granularity and the alumina particle granularity of high-temperature agglomerant can not differ too large, otherwise in sintering process during high-temperature agglomerant melting, some hole around high-temperature agglomerant will be closed by glassy phase, forms closed pores and loses, causing effective void content to decline.
Preferred as one, mixed clay is mass ratio is (6-10): the feldspar of (6-8): 3:1, kaolinite, raw talcum and montmorillonite mixture.Feldspar is a kind of aluminium silicate mineral containing calcium, sodium, potassium, can expand the sintering range of pottery, but the alkalimetal oxide in feldspar can reduce the physical strength of porcelain base, therefore should be controlled.When sintering temperature is higher than 1100 DEG C, feldspar starts to form liquid phase, form glass gradually to combine in blapharoplast junction, impurity now in kaolinite, raw talcum and montmorillonite reaches the ratio of eutectic mixture, also starts to form liquid phase, and kaolinite, raw talcum and montmorillonite particle not only form Ceramic bond with feldspar, also form glass with Membranes On Alumina Particles Surface to be combined, reduce the mobility of feldspar simultaneously to a certain extent, both ensure that sintering, and turn avoid blank deformation.
Add the rare earth oxide of 2-5%, such as lanthanum trioxide, cerium oxide, Praseodymium trioxide, all obviously can improve microstructure and the performance of alumina ceramic material, wherein lanthanum, cerium, praseodymium element are surface active elements, when its oxide particle and blapharoplast meet, tend to be distributed in blapharoplast surface, the impurity of absorption grain boundaries, purification crystal boundary.Rare earth oxide particles and alumina particle contact reacts form low melting point liquid phase in addition, obviously can reduce the sintering temperature of pottery.When rare earth oxide content lower than 2% time, sintering temperature reduces not obvious, affect the surfactivity of cleaner, and content higher than 5% time, porosity can be caused greatly to reduce, and be unfavorable for the specific surface area of increase stupalith, therefore its content there is no need to be greater than 5%.
Preferred as one, fortifying fibre is the one in silicon carbide fiber or carbon fiber.Due to the Embrittlement of stupalith, make stupalith at high temperature, heavily stressed, the application particularly under dynamic condition is restricted.And silicon carbide fiber and carbon fiber strength is high, modulus is high, density is low, stable chemical performance, thermal expansivity are little, there is good high thermal resistance, be subject in the process of foreign impacts at stupalith, silicon carbide fiber and carbon fiber can change crackle the evolving path, absorb energy to fracture, the connection transboundary to different crystal boundary, crystallizing field and impurity defect region can also be realized, thus reach the object improving stupalith fragility, intensified ceramic material.Described fortifying fibre is through plasma surface pretreated.Silicon carbide fiber and carbon fiber surface inertia larger, poor with the consistency of ceramic matrix, easily on interface, form hole and defect, cause with the bonding strength at interface lower.Use Cement Composite Treated by Plasma mainly by plasma strike fiber surface, thus etching fiber sheath, the roughness on its surface is increased, and surface-area is corresponding increase also, significantly increases so the wetting property of fiber in ceramic matrix has; Cement Composite Treated by Plasma silicon carbide fiber and carbon fiber can make its degree of graphitization and regularity reduce simultaneously, increase, so cohesiveness also increases with the mechanical twisting point of ceramic matrix; Cement Composite Treated by Plasma also can form radical at fiber surface, improves interface binding power, improves mechanical property.
A preparation method for exhaust purifier, comprises the steps:
1) ceramic size preparation: alumina powder jointed, sintering aid, mixed clay, rare earth oxide are mixed and obtain mixed powder, by mixed powder with solvent with (80-85): the mass ratio of 100 fully mixes, add fortifying fibre again, be uniformly dispersed and obtain ceramic size;
2) shaping base, obtains biscuit; Being embodied as step 1 of this step) gained slurry undertaken by extrusion equipment;
3) sinter: biscuit regulates pressure to 20MPa in 1100-1200 DEG C of sintering 60-90min, b. by a. at ambient pressure, adjust the temperature to 800-1000 DEG C of continuation sintering 30-60min, c. and be incubated 90-120min at 500-700 DEG C, obtain honeycomb ceramic carrier;
4) carrier coating and dipping: pulp solution is coated on obtained honeycomb ceramic carrier surface, after drying process, the active component solution put into by carrier containing palladium, platinum, rhodium carries out dip treating again;
5) subsequent disposal: by step 4) the carrier drying that obtains and calcination process (put into stoving oven and carry out adding thermal bake-out by following temperature curve, time controling is at 5-8h: one district: 170-190 DEG C, 2nd district: 200-240 DEG C, 3rd district: 280-320 DEG C, 4th district: 370-500 DEG C, 5th district: 500-520 DEG C) after carrier and housing are assembled, make complete exhaust purifier.Carrier carries out adding thermal bake-out according to temperature curve, carrier is heated and compares uniform speed slow, moisture can be removed equably, temperature distributing disproportionation can not be caused to make active coating ftracture or come off because heating up suddenly, it also avoid the deformation and damage of base substrate in roasting process simultaneously, and in this temperature profile range, the components such as palladium, platinum, rhodium also can keep maximum activity can not inactivation.
, step 4 preferred as one) coating is divided into and completes for twice, and wherein the wet weightening finish of second time coating is than first time heavy 45-55% (coating here wet weightening finish refer to the increasing amount of carrier quality after coating).
, step 4 preferred as one) carrier percentage of plugged hole after coating is less than 1%.If there is plug-hole phenomenon, be then less than 1% (number in hole that percentage of plugged hole is here blocked after referring to carrier coating and the ratio of total hole count) with air gun purging to percentage of plugged hole.
Beneficial effect of the present invention: adopt the exhaust purifier that technique scheme is obtained; its honeycomb ceramic carrier ultimate compression strength is high, thermal expansivity is little, sintering temperature is low; be a kind of alumina ceramic carrier optimizing modification, its preparation method is simply efficient, is applicable to large-scale production.
Embodiment
Below in conjunction with embodiment, illustrate the present invention further, following embodiment should be understood and be only not used in for illustration of the present invention and limit the scope of the invention.
Exhaust purifier disclosed by the invention, comprise housing and honeycomb ceramic carrier, honeycomb ceramic carrier is arranged in housing, the vesicular structure of described honeycomb ceramic carrier comprises bending serpentine channel and straight way, and straight way is communicated on serpentine channel, and component and the massfraction thereof of described honeycomb ceramic carrier comprise: sintering aid: 6-10%, mixed clay: 2-5%, rare earth oxide: 2-5%, fortifying fibre: 1-2%, surplus is alumina powder jointed.
Preferred as one, the aperture ratio of straight way and serpentine channel is 4:(4-5).
Preferred as one, described straight way is (5-6) with the pore volume ratio of serpentine channel: (4-5).
Preferred as one, described alumina powder jointed particle diameter is 150-200nm.
Preferred as one, described sintering aid is MgO, CaO, SiO
2, V
2o
5, Fe
2o
3, TiO
2in at least two kinds.
Preferred as one, described mixed clay is pretreated through 1400 DEG C of high temperature.
Preferred as one, described mixed clay is mass ratio is (6-10): the feldspar of (6-8): 3:1, kaolinite, raw talcum and montmorillonite mixture.
Preferred as one, described fortifying fibre is the one in silicon carbide fiber or carbon fiber.
The preparation method of exhaust purifier of the present invention, comprises the steps:
1) ceramic size preparation: alumina powder jointed, sintering aid, mixed clay, rare earth oxide are mixed and obtain mixed powder, by mixed powder with solvent with (80-85): the mass ratio of 100 fully mixes, add fortifying fibre again, be uniformly dispersed and obtain ceramic size;
2) shaping base, obtains biscuit;
3) sinter: after biscuit is sintered 60-90min in 1100-1200 DEG C by a. at ambient pressure, b. regulate pressure to 20MPa, adjust the temperature to 800-1000 DEG C of continuation sintering 30-60min, c. and at 500-700 DEG C, be incubated 90-120min again, obtain honeycomb ceramic carrier;
4) carrier coating and dipping: pulp solution is coated on obtained honeycomb ceramic carrier surface, after drying process, the active component solution put into by carrier containing palladium, platinum, rhodium carries out dip treating again;
5) subsequent disposal: by step 4) assemble with housing after the carrier drying that obtains and calcination process, make exhaust purifier.
Described step 4) coating is divided into and completes for twice, the wherein wet weightening finish of second time coating 45-55% heavier than first time.
Embodiment 1
The exhaust purifier of the present embodiment, comprise housing and honeycomb ceramic carrier, honeycomb ceramic carrier is arranged in housing, the vesicular structure of described honeycomb ceramic carrier comprises bending serpentine channel and straight way, and straight way is communicated on serpentine channel, and component and the massfraction thereof of described honeycomb ceramic carrier comprise: sintering aid: 6%, mixed clay: 4%, rare earth oxide: 5%, silicon carbide fiber: 2%, all the other 83% are alumina powder jointed.Wherein MgO and CaO of sintering aid to be mass ratio be 1:1, the feldspar of mixed clay to be mass ratio be 6:6:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide; Wherein silicon carbide fiber is (this place pretreating scheme can also be applicable to include, without being limited to the present invention and enumerate other embodiment in interior all technical schemes) through argon plasma surface preparation.Wherein the aperture ratio of straight way and serpentine channel is 1:1, and pore volume is than being 5:4.
Embodiment 2
The exhaust purifier of the present embodiment, comprise housing and honeycomb ceramic carrier, honeycomb ceramic carrier is arranged in housing, the vesicular structure of described honeycomb ceramic carrier comprises bending serpentine channel and straight way, and straight way is communicated on serpentine channel, and component and the massfraction thereof of described honeycomb ceramic carrier comprise: sintering aid: 7%, mixed clay: 2%, rare earth oxide: 4%, carbon fiber: 2%, all the other 85% are alumina powder jointed.Wherein MgO, SiO of sintering aid to be mass ratio be 2:1:1
2and Fe
2o
3the feldspar of mixed clay to be mass ratio be 7:8:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide; Wherein silicon carbide fiber is (this place pretreating scheme can also be applicable to include, without being limited to the present invention and enumerate other embodiment in interior all technical schemes) through argon plasma surface preparation.Wherein the aperture ratio of straight way and serpentine channel is 4:5, and pore volume is than being 1:1.
Embodiment 3
The exhaust purifier of the present embodiment, comprise housing and honeycomb ceramic carrier, honeycomb ceramic carrier is arranged in housing, the vesicular structure of described honeycomb ceramic carrier comprises bending serpentine channel and straight way, and straight way is communicated on serpentine channel, and component and the massfraction thereof of described honeycomb ceramic carrier comprise: sintering aid: 9%, mixed clay: 5%, rare earth oxide: 2%, carbon fiber: 1.5%, all the other 82.5% are alumina powder jointed.Wherein CaO, V of sintering aid to be mass ratio be 2:2:1:1
2o
5, Fe
2o
3and TiO
2the feldspar of mixed clay to be mass ratio be 8:8:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide.Wherein the aperture ratio of straight way and serpentine channel is 4:4.5, and pore volume is than being 3:2.
Embodiment 4
The exhaust purifier of the present embodiment, comprise housing and honeycomb ceramic carrier, honeycomb ceramic carrier is arranged in housing, the vesicular structure of described honeycomb ceramic carrier comprises bending serpentine channel and straight way, and straight way is communicated on serpentine channel, and component and the massfraction thereof of described honeycomb ceramic carrier comprise: sintering aid: 8%, mixed clay: 5%, rare earth oxide: 3%, silicon carbide fiber: 1%, all the other 83% are alumina powder jointed.Wherein MgO, CaO, V of sintering aid to be mass ratio be 3:1:1:1
2o
5and TiO
2the feldspar of mixed clay to be mass ratio be 9:7:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide.Wherein the aperture ratio of straight way and serpentine channel is 4:4.2, and pore volume is than being 6:5.
Embodiment 5
The exhaust purifier of the present embodiment, comprise housing and honeycomb ceramic carrier, honeycomb ceramic carrier is arranged in housing, the vesicular structure of described honeycomb ceramic carrier comprises bending serpentine channel and straight way, and straight way is communicated on serpentine channel, and component and the massfraction thereof of described honeycomb ceramic carrier comprise: sintering aid: 10%, mixed clay: 3%, rare earth oxide: 5%, carbon fiber: 1.5%, all the other 80.5% are alumina powder jointed.Wherein MgO, CaO, SiO of sintering aid to be mass ratio be 1:1:1:1:1:1
2, V
2o
5, Fe
2o
3and TiO
2the feldspar of mixed clay to be mass ratio be 10:8:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide.Wherein the aperture ratio of straight way and serpentine channel is 4:4.6, and pore volume is than being 5:4.
The difference of embodiment 6-10 and embodiment 1-5 be only described alumina powder jointed particle diameter be respectively 200,160,175,180,150nm.
The difference of embodiment 11-15 and embodiment 6-10 is only that described mixed clay is for pretreated (in this place embodiment, the high temperature pretreated time is 5min through 1400 DEG C of high temperature.Pretreatment time can also be 6,7,8,9, other random time values between 10min and 5-10min.This place pretreating scheme can also be applicable to include, without being limited to the present invention and enumerate other embodiment in interior all technical schemes).
Embodiment 16
The preparation method of the present embodiment exhaust purifier, step is as follows:
1) ceramic size preparation: alumina powder jointed, sintering aid, mixed clay, rare earth oxide are mixed and obtain mixed powder, mixed powder is fully mixed with the mass ratio of 80:100 with ethanolic soln, add silicon carbide fiber again, be uniformly dispersed and obtain ceramic size;
Wherein alumina powder jointed, sintering aid, mixed clay, rare earth oxide and silicon carbide fiber mass ratio is 85:7:3:4:1, wherein MgO and CaO of sintering aid to be mass ratio be 1:1, the feldspar of mixed clay to be mass ratio be 6:6:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide;
2) slurry is passed through the shaping base of extrusion shaping machine, obtain biscuit;
3) sinter: a. is by biscuit at ambient pressure after 1100 DEG C of sintering 60min, and b. regulates pressure to 20MPa, adjust the temperature to 800 DEG C of continuation sintering 30min, c. and at 700 DEG C, be incubated 90min again, obtain honeycomb ceramic carrier;
4) carrier coating and dipping: pulp solution is coated on obtained honeycomb ceramic carrier surface, after drying process, the active component solution put into by carrier containing palladium, platinum, rhodium carries out dip treating again; Wherein apply to be divided into and complete for twice, second time coating wet weightening finish ratio first time weighs 55%, and the carrier percentage of plugged hole after coating is less than 1%.
5) subsequent disposal: by step 4) assemble with housing after the carrier drying that obtains and calcination process, make exhaust purifier.
Embodiment 17
The preparation method of the present embodiment exhaust purifier, step is as follows:
1) ceramic size preparation: alumina powder jointed, sintering aid, mixed clay, rare earth oxide are mixed and obtain mixed powder, mixed powder is fully mixed with the mass ratio of 81:100 with ethanolic soln, add carbon fiber again, be uniformly dispersed and obtain ceramic size;
Wherein alumina powder jointed, sintering aid, mixed clay, rare earth oxide and carbon fiber mass ratio is 82:9:4:4:1, wherein MgO and Fe of sintering aid to be mass ratio be 1:1
2o
3the feldspar of mixed clay to be mass ratio be 7:8:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide;
2) slurry is passed through the shaping base of extrusion shaping machine, obtain biscuit;
3) sinter: a. is by biscuit at ambient pressure after 1100 DEG C of sintering 65min, and b. regulates pressure to 20MPa, adjust the temperature to 1000 DEG C of continuation sintering 40min, c. and at 650 DEG C, be incubated 100min again, obtain honeycomb ceramic carrier;
4) carrier coating and dipping: pulp solution is coated on obtained honeycomb ceramic carrier surface, after drying process, the active component solution put into by carrier containing palladium, platinum, rhodium carries out dip treating again; Wherein apply to be divided into and complete for twice, second time coating wet weightening finish ratio first time weighs 52%, and the carrier percentage of plugged hole after coating is less than 1%.
5) subsequent disposal: by step 4) assemble with housing after the carrier drying that obtains and calcination process, make exhaust purifier.
Embodiment 18
The preparation method of the present embodiment exhaust purifier, step is as follows:
1) ceramic size preparation: alumina powder jointed, sintering aid, mixed clay, rare earth oxide are mixed and obtain mixed powder, mixed powder is fully mixed with the mass ratio of 83:100 with ethanolic soln, add silicon carbide fiber again, be uniformly dispersed and obtain ceramic size;
Wherein alumina powder jointed, sintering aid, mixed clay, rare earth oxide and silicon carbide fiber mass ratio is 84:7:4:3:2, wherein CaO, V of sintering aid to be mass ratio be 2:2:1
2o
5and Fe
2o
3the feldspar of mixed clay to be mass ratio be 8:8:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide;
2) slurry is passed through the shaping base of extrusion shaping machine, obtain biscuit;
3) sinter: a. is by biscuit at ambient pressure after 1200 DEG C of sintering 75min, and b. regulates pressure to 20MPa, adjust the temperature to 900 DEG C of continuation sintering 45min, c. and at 600 DEG C, be incubated 110min again, obtain honeycomb ceramic carrier;
4) carrier coating and dipping: pulp solution is coated on obtained honeycomb ceramic carrier surface, after drying process, the active component solution put into by carrier containing palladium, platinum, rhodium carries out dip treating again; Wherein apply to be divided into and complete for twice, second time coating wet weightening finish ratio first time weighs 49%, and the carrier percentage of plugged hole after coating is less than 1%.
5) subsequent disposal: by step 4) assemble with housing after the carrier drying that obtains and calcination process, make exhaust purifier.
Embodiment 19
The preparation method of the present embodiment exhaust purifier, step is as follows:
1) ceramic size preparation: alumina powder jointed, sintering aid, mixed clay, rare earth oxide are mixed and obtain mixed powder, mixed powder is fully mixed with the mass ratio of 84:100 with ethanolic soln, add carbon fiber again, be uniformly dispersed and obtain ceramic size;
Wherein alumina powder jointed, sintering aid, mixed clay, rare earth oxide and carbon fiber mass ratio is 81:10:3:4:2, wherein MgO, V of sintering aid to be mass ratio be 3:1:1
2o
5and TiO
2the feldspar of mixed clay to be mass ratio be 9:7:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide;
2) slurry is passed through the shaping base of extrusion shaping machine, obtain biscuit;
3) sinter: a. is by biscuit at ambient pressure after 1150 DEG C of sintering 80min, and b. regulates pressure to 20MPa, adjust the temperature to 900 DEG C of continuation sintering 55min, c. and at 550 DEG C, be incubated 110min again, obtain honeycomb ceramic carrier;
4) carrier coating and dipping: pulp solution is coated on obtained honeycomb ceramic carrier surface, after drying process, the active component solution put into by carrier containing palladium, platinum, rhodium carries out dip treating again; Wherein apply to be divided into and complete for twice, second time coating wet weightening finish ratio first time weighs 46%, and the carrier percentage of plugged hole after coating is less than 1%.
5) subsequent disposal: by step 4) assemble with housing after the carrier drying that obtains and calcination process, make exhaust purifier.
Embodiment 20
The preparation method of the present embodiment exhaust purifier, step is as follows:
1) ceramic size preparation: alumina powder jointed, sintering aid, mixed clay, rare earth oxide are mixed and obtain mixed powder, mixed powder is fully mixed with the mass ratio of 85:100 with ethanolic soln, add carbon fiber again, be uniformly dispersed and obtain ceramic size;
Wherein alumina powder jointed, sintering aid, mixed clay, rare earth oxide and carbon fiber mass ratio is 81:8:5:5:1, wherein MgO and TiO of sintering aid to be mass ratio be 1:1
2the feldspar of mixed clay to be mass ratio be 10:8:3:1, kaolinite, raw talcum and montmorillonite mixture, rare earth oxide can be one or both and two or more mixtures in the rare earth oxides such as lanthanum trioxide, cerium oxide, rubidium oxide, Praseodymium trioxide, dysprosium oxide, promethium oxide;
2) slurry is passed through the shaping base of extrusion shaping machine, obtain biscuit;
3) sinter: a. is by biscuit at ambient pressure after 1150 DEG C of sintering 90min, and b. regulates pressure to 20MPa, adjust the temperature to 950 DEG C of continuation sintering 60min, c. and at 500 DEG C, be incubated 120min again, obtain honeycomb ceramic carrier;
4) carrier coating and dipping: pulp solution is coated on obtained honeycomb ceramic carrier surface, after drying process, the active component solution put into by carrier containing palladium, platinum, rhodium carries out dip treating again; Wherein apply to be divided into and complete for twice, second time coating wet weightening finish ratio first time weighs 45%, and the carrier percentage of plugged hole after coating is less than 1%.
5) subsequent disposal: by step 4) assemble with housing after the carrier drying that obtains and calcination process, (calcination process technique carries out adding thermal bake-out for dried carrier being put into stoving oven by following temperature curve to make exhaust purifier, time controling is at 5h: one district: 170-190 DEG C, 2nd district: 200-240 DEG C, 3rd district: 280-320 DEG C, 4th district: 370-500 DEG C, 5th district: 500-520 DEG C.Roasting time can also be 5.1,5.1,5.3,5.5,5.7,5.9,6,7, other random times between 8h and 5-8h.This place pretreating scheme can also be applicable to include, without being limited to the present invention and enumerate other embodiment in interior all technical schemes).
The honeycomb ceramic carrier getting each embodiment measures its thermal expansivity and ultimate compression strength according to GB/T25994-2010, and wherein the test data of embodiment 5,10,15,20 lists in table 1.
Comparative example
Take mass ratio as alumina powder jointed, the SiO of 49:33:13
2be that raw material makes honeycomb ceramic carrier according to common method for making with MgO, then measure its thermal expansivity and ultimate compression strength according to GB/T25994-2010, the data obtained lists in table 1.
Table 1
After measured, thermal expansivity is all not more than 1.20 × 10 to each embodiment gained honeycomb ceramic carrier above
-6dEG C
-1, ultimate compression strength A direction of principal axis is all not less than 15.0MPa, and B direction of principal axis is all not less than 4.5MPa, and C direction of principal axis is all not less than 0.8MPa.
In view of the present invention program's embodiment is numerous, each embodiment experimental data is huge numerous, be not suitable for particularize herein to illustrate, but the content of the required checking of each embodiment is all close with the final conclusion obtained, so do not illustrate one by one the checking content of each embodiment herein.
The technical scope mid point value non-limit part that this place embodiment is protected application claims and in embodiment technical scheme to the new technical scheme that the equal replacement of single or multiple technical characteristic is formed, equally all in the scope of protection of present invention; Simultaneously in all embodiments enumerated or do not enumerate of the present invention program, parameters in the same embodiment only represents an example (i.e. a kind of feasible scheme) of its technical scheme, and between parameters, there is not strict cooperation and qualified relation, wherein each parameter can be replaced, except special declaration mutually when stating ask without prejudice to axiom and the present invention.
Technique means disclosed in the present invention program is not limited only to the technique means disclosed in above-mentioned technique means, also comprises the technical scheme be made up of above technical characteristic arbitrary combination.The above is the specific embodiment of the present invention; it should be pointed out that for those skilled in the art, under the premise without departing from the principles of the invention; can also make some improvements and modifications, these improvements and modifications are also considered as protection scope of the present invention.
Claims (10)
1. an exhaust purifier, comprise housing and honeycomb ceramic carrier, honeycomb ceramic carrier is arranged in housing, it is characterized in that: the vesicular structure of described honeycomb ceramic carrier comprises bending serpentine channel and straight way, and straight way is communicated on serpentine channel, component and the massfraction thereof of described honeycomb ceramic carrier comprise: sintering aid: 6-10%, mixed clay: 2-5%, rare earth oxide: 2-5%, fortifying fibre: 1-2%, surplus is alumina powder jointed.
2. exhaust purifier according to claim 1, is characterized in that: the aperture ratio of described straight way and serpentine channel is 4:(4-5).
3. exhaust purifier according to claim 1 and 2, is characterized in that: described straight way is (5-6) with the pore volume ratio of serpentine channel: (4-5).
4. exhaust purifier according to claim 1, is characterized in that: described alumina powder jointed particle diameter is 150-200nm.
5. exhaust purifier according to claim 1, is characterized in that: described sintering aid is MgO, CaO, SiO
2, V
2o
5, Fe
2o
3, TiO
2in at least two kinds.
6. exhaust purifier according to claim 1, is characterized in that: described mixed clay is for pretreated through 1400 DEG C of high temperature.
7. the exhaust purifier according to claim 1 or 6, is characterized in that: described mixed clay is mass ratio is (6-10): the feldspar of (6-8): 3:1, kaolinite, raw talcum and montmorillonite mixture.
8. exhaust purifier according to claim 1, is characterized in that: described fortifying fibre is the one in silicon carbide fiber or carbon fiber.
9. a preparation method for exhaust purifier, is characterized in that comprising the steps:
1) ceramic size preparation: alumina powder jointed, sintering aid, mixed clay, rare earth oxide are mixed and obtain mixed powder, by mixed powder with solvent with (80-85): the mass ratio of 100 fully mixes, add fortifying fibre again, be uniformly dispersed and obtain ceramic size;
2) shaping base, obtains biscuit;
3) sinter: after biscuit is sintered 60-90min in 1100-1200 DEG C by a. at ambient pressure, b. regulate pressure to 20MPa, adjust the temperature to 800-1000 DEG C of continuation sintering 30-60min, c. and at 500-700 DEG C, be incubated 90-120min again, obtain honeycomb ceramic carrier;
4) carrier coating and dipping: pulp solution is coated on obtained honeycomb ceramic carrier surface, after drying process, the active component solution put into by carrier containing palladium, platinum, rhodium carries out dip treating again;
5) subsequent disposal: by step 4) assemble with housing after the carrier drying that obtains and calcination process, make exhaust purifier.
10. the preparation method of exhaust purifier according to claim 9, is characterized in that: described step 4) coating is divided into and completes for twice, the wherein wet weightening finish of second time coating 45-55% heavier than first time.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510799273.1A CN105367114A (en) | 2015-11-19 | 2015-11-19 | Exhaust purifier and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510799273.1A CN105367114A (en) | 2015-11-19 | 2015-11-19 | Exhaust purifier and preparation method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105367114A true CN105367114A (en) | 2016-03-02 |
Family
ID=55369819
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510799273.1A Pending CN105367114A (en) | 2015-11-19 | 2015-11-19 | Exhaust purifier and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105367114A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109224757A (en) * | 2018-11-22 | 2019-01-18 | 湖南工业大学 | A kind of gasification of biomass liquefaction organic tail gas clarifier and preparation method thereof |
| CN109721343A (en) * | 2019-01-17 | 2019-05-07 | 东莞信柏结构陶瓷股份有限公司 | Porous ceramics raw material, porous ceramics and the preparation method and application thereof |
| CN112657335A (en) * | 2020-12-17 | 2021-04-16 | 宁波科森净化器制造有限公司 | Exhaust gas purifier with strong-binding-force composite coating |
| CN113171783A (en) * | 2021-04-21 | 2021-07-27 | 中化环境科技工程有限公司 | Microporous honeycomb ozone catalyst and preparation method and application thereof |
| CN114671679A (en) * | 2022-04-11 | 2022-06-28 | 武汉科技大学 | Zirconium pyrophosphate complex phase ceramic material and preparation method thereof |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103742231A (en) * | 2013-12-23 | 2014-04-23 | 柳州正菱集团有限公司 | Automobile exhaust purifier device |
| CN104072111A (en) * | 2013-03-29 | 2014-10-01 | 北京市理化分析测试中心 | Preparation method of aluminium oxide honeycomb ceramics |
-
2015
- 2015-11-19 CN CN201510799273.1A patent/CN105367114A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104072111A (en) * | 2013-03-29 | 2014-10-01 | 北京市理化分析测试中心 | Preparation method of aluminium oxide honeycomb ceramics |
| CN103742231A (en) * | 2013-12-23 | 2014-04-23 | 柳州正菱集团有限公司 | Automobile exhaust purifier device |
Non-Patent Citations (1)
| Title |
|---|
| 胡昌义等: "《贵金属新材料》", 30 September 2015 * |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109224757A (en) * | 2018-11-22 | 2019-01-18 | 湖南工业大学 | A kind of gasification of biomass liquefaction organic tail gas clarifier and preparation method thereof |
| CN109721343A (en) * | 2019-01-17 | 2019-05-07 | 东莞信柏结构陶瓷股份有限公司 | Porous ceramics raw material, porous ceramics and the preparation method and application thereof |
| CN112657335A (en) * | 2020-12-17 | 2021-04-16 | 宁波科森净化器制造有限公司 | Exhaust gas purifier with strong-binding-force composite coating |
| CN113171783A (en) * | 2021-04-21 | 2021-07-27 | 中化环境科技工程有限公司 | Microporous honeycomb ozone catalyst and preparation method and application thereof |
| CN113171783B (en) * | 2021-04-21 | 2023-03-21 | 中化环境科技工程有限公司 | Microporous honeycomb ozone catalyst and preparation method and application thereof |
| CN114671679A (en) * | 2022-04-11 | 2022-06-28 | 武汉科技大学 | Zirconium pyrophosphate complex phase ceramic material and preparation method thereof |
| CN114671679B (en) * | 2022-04-11 | 2023-04-18 | 武汉科技大学 | Zirconium pyrophosphate complex phase ceramic material and preparation method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105367114A (en) | Exhaust purifier and preparation method thereof | |
| CN110614101A (en) | Catalyst for catalytic combustion of VOCs and preparation method thereof | |
| CN103586016B (en) | Honeycomb fashion denitrifying catalyst with selective catalytic reduction and preparation method thereof | |
| JP5752418B2 (en) | Method for producing honeycomb-type catalyst for reducing nitrogen oxides, and method for treating nitrogen oxide exhaust gas | |
| CN105944665A (en) | Preparation method of molecular sieve concentration rotating wheel adsorption packing for treating VOCs | |
| CN105399433A (en) | Purifier and preparation method thereof | |
| CA2651503A1 (en) | Hydrothermally stable alumina | |
| US5034369A (en) | Novel catalysts for the treatment of gaseous effluents containing oxidizable sulfur pollutants | |
| CN108499556B (en) | Low-temperature denitration catalyst and preparation method thereof | |
| CN103011840A (en) | Preparation method for ultrafine fused silica powder used in automobile honeycomb ceramic carrier | |
| CN108546105A (en) | A kind of high-strength tenacity graphene composite ceramics | |
| CN104529506A (en) | Preparation method of compound natural porous mineral ceramic microbeads | |
| CN106669670A (en) | Preparation method of flue gas desulfurization agent | |
| CN105367112A (en) | Vehicle exhaust purifier and preparation method thereof | |
| CN105367123A (en) | Motor vehicle exhaust purifier and preparation method thereof | |
| CN105399406A (en) | Exhaust purifier for automobile and preparation method of exhaust purifier | |
| IE903596A1 (en) | Catalysts for treating gaseous effluent and a method of¹treating the effluent | |
| CN112592186A (en) | Porous ceramic for filtering flue gas and preparation method and application thereof | |
| CN104368334A (en) | Denitration catalyst and its preparation method | |
| CN101474570A (en) | SCR granular catalyst substrate and preparation method thereof | |
| KR101187758B1 (en) | METHOD FOR MANUFACTURING DE-NOx SCR CATALYST USING CALCIUM SULFATE HEMIHYDRATE | |
| CN103706406B (en) | Composite support for denitration catalyst and preparation method of composite support | |
| CN105435765A (en) | Preparation method of denitration catalyst | |
| CN108675823A (en) | A kind of diesel emission particulate purification DPF honeycomb ceramic carriers | |
| CN107199014A (en) | A kind of ceramic composition of high absorption property 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 | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160302 |