CN102389797A - Auto catalyst and preparation method thereof - Google Patents
Auto catalyst and preparation method thereof Download PDFInfo
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- CN102389797A CN102389797A CN2011103228410A CN201110322841A CN102389797A CN 102389797 A CN102389797 A CN 102389797A CN 2011103228410 A CN2011103228410 A CN 2011103228410A CN 201110322841 A CN201110322841 A CN 201110322841A CN 102389797 A CN102389797 A CN 102389797A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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Abstract
The invention discloses an auto catalyst and a preparation method thereof. The catalyst is characterized by being prepared by taking cordierite honeycomb ceramic as a carrier and a Ce-Zr-La composite oxide and BaO as auxiliaries and loading an active ingredient Pd. The catalyst has higher rate of conversion of NO, CO and HC seriously polluting the air in the auto exhaust without actions of other substances and has low toxicity and high catalytic activity.
Description
Technical field
The present invention relates to a kind of automobile catalyst and preparation method thereof, is that it is to polluter NO in the vehicle exhaust specifically
X, HC and CO carry out the catalyst and the synthetic technology thereof of integrated treatment.
Background technology
Automobile has become requisite part in our daily life.Automobile has also produced many bad accessory substances bringing us simultaneously easily.Tail gas pollution is exactly one of accessory substance, also is one of main source of atmosphere pollution simultaneously.Most NO in the city
X, CO, HC and CO
2All make CO by vehicle exhaust
2Cause the one of the main reasons of atmosphere pollution and greenhouse effects especially.NO
X, CO, HC not only cause damage but also produce blue photochemical fog under certain conditions human body, makes vegetation dead, the environment of human survival is destroyed.
At present, the major measure of control motor vehicle exhaust emission is to develop the purification techniques of auto-exhaust catalyst efficiently.Currently use maximum auto-exhaust catalysts to be noble metal triple effect catalyst (TWC), noble metal catalyst has higher activity, and big extremely ratio is occupied in tail-gas catalyst market in the world, but itself also has a lot of shortcomings.Have only when the scope of air-fuel ratio is controlled at (14.6 ± 0.3), just can make NO
X, CO and HC detergent power reach maximum, outside this scope, catalytic effect is all relatively poor.Noble metal catalyst was poisoned when elements such as Pb, S, P all were prone to, wherein Pb having the greatest impact to TWC.The price of noble metal is expensive, and the noble metal scarcity of resources also makes the application of TW C and popularization be restricted at present.
Summary of the invention
The objective of the invention is to the costing an arm and a leg of noble metal in the prior art, shortcoming such as toxicity is big provides the little activity of a kind of toxicity higher auto-exhaust catalyst.
Technical scheme of the present invention is: a kind of automobile catalyst, this catalyst are carrier with the cordierite honeycomb ceramic, and Ce-Zr-La composite oxides and BaO are auxiliary agent, and supported active composition Pd processes.Described component Ce-Zr-La composite oxides, BaO, Pd are 1 ~ 5:3 ~ 8:1 ~ 3 at the load capacity proportion by weight of integer catalyzer.
The preparation method of automobile catalyst comprises the steps:
A is that the ratio of 1 ~ 5:3 ~ 8 adds the deionized water of press amount of the mixture 20% ~ 50% with Ce-Zr-La composite oxides and BaO according to mass ratio, and in the adding ball grinder, ball milling 3 ~ 6h processes slurry;
B immerses cordierite honeycomb ceramic carrier in the slurry, takes out behind 1 ~ 5min, dries, and dries by the fire 3 ~ 6h at a certain temperature;
C is immersed in the PdCl that contains Pd1 ~ 3g/L with the carrier of oven dry
2In the ammonia solution, stir 3 ~ 6h, take out, dry, dry by the fire 3 ~ 6h at a certain temperature;
D immerses KBH with the carrier of oven dry
4In the solution, reaction 10 ~ 50min spends deionised water, at room temperature carries out chemical plating again, and reaction 10 ~ 50min is washed till neutrality with deionized water, at a certain temperature oven dry.
It is short that the present invention has overcome the conventional catalysts life-span, is prone to poison, and confirming of poor stability realized long-acting, stable high, safe.
The present invention has adopted the method for chemical plating, and it is simple that more traditional technology has an equipment, invest lowly, and chemical plating coating is even, and the hardness height resistance to wears, and is corrosion-resistant.
Description of drawings
Fig. 1 catalyst is to NO
X, CO and HC conversion ratio be with temperature changing curve diagram.
The specific embodiment
Instance 1 Ce-Zr-La composite oxides, BaO and Pd/ cordierite are synthetic:
Is the deionized water of the ratio adding of 3:4 by amount of the mixture 30% with Ce-Zr-La composite oxides and BaO according to mass ratio, adds in the ball grinder, and ball milling 5h processes slurry.Cordierite honeycomb ceramic carrier is immersed in the slurry, take out behind the 2min, dry, dry by the fire 4h down at 115 ℃.The carrier of oven dry is immersed in the PdCl that contains Pd2.2g/L
2In the ammonia solution, stir 4h.Take out, dry, dry by the fire 4h at a certain temperature.The carrier of oven dry is immersed KBH
4In the solution, reaction 30min spends deionised water, at room temperature carries out chemical plating again, and reaction 30min is washed till neutrality with deionized water, dries down at 115 ℃ and obtains Ce-Zr-La composite oxides, BaO and Pd/ cordierite.
Instance 2 catalyst are investigated the catalytic activity of vehicle exhaust:
With the prepared catalyst of instance 1 to the NO in the vehicle exhaust
X, CO and HC conversion ratio investigate.Test is in high temperature reaction stove, to carry out.To contain NO, CO
2, H
2Gaseous mixture feed in the high temperature reaction stove, every min heats up 10 ℃, finally rises to 500 ℃.Experimental result is seen table 1 and Fig. 1.
Table 1
Claims (3)
1. an automobile catalyst is characterized in that it is is carrier with the cordierite honeycomb ceramic, and Ce-Zr-La composite oxides and BaO are auxiliary agent, and supported active composition Pd processes; Described component Ce-Zr-La composite oxides, BaO, Pd are 1 ~ 5:3 ~ 8:1 ~ 3 at the load capacity proportion by weight of integer catalyzer.
2. the preparation method of automobile catalyst according to claim 1 is characterized in that comprising the steps:
A is that the ratio of 1 ~ 5:3 ~ 8 adds the deionized water of press amount of the mixture 20% ~ 50% with Ce-Zr-La composite oxides and BaO according to mass ratio, and in the adding ball grinder, ball milling 3 ~ 6h processes slurry;
B immerses cordierite honeycomb ceramic carrier in the slurry, takes out behind 1 ~ 5min, dries, and dries by the fire 3 ~ 6h at a certain temperature;
C is immersed in the PdCl that contains Pd1 ~ 3g/L with the carrier of oven dry
2In the ammonia solution, stir 3 ~ 6h, take out, dry, dry by the fire 3 ~ 6h at a certain temperature;
D immerses KBH with the carrier of oven dry
4In the solution, reaction 10 ~ 50min spends deionised water, at room temperature carries out chemical plating again, and reaction 10 ~ 50min is washed till neutrality with deionized water, at a certain temperature oven dry.
3. the preparation method of automobile catalyst according to claim 2 is characterized in that: after the d step supported catalyst active ingredient is peeled off into powder or processed solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2011103228410A CN102389797A (en) | 2011-10-21 | 2011-10-21 | Auto catalyst and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2011103228410A CN102389797A (en) | 2011-10-21 | 2011-10-21 | Auto catalyst and preparation method thereof |
Publications (1)
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CN102389797A true CN102389797A (en) | 2012-03-28 |
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CN2011103228410A Pending CN102389797A (en) | 2011-10-21 | 2011-10-21 | Auto catalyst and preparation method thereof |
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- 2011-10-21 CN CN2011103228410A patent/CN102389797A/en active Pending
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Application publication date: 20120328 |