CN1194182A - Fluid fuel reforming ceramic catalysts and their manufacturing methods - Google Patents
Fluid fuel reforming ceramic catalysts and their manufacturing methods Download PDFInfo
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- CN1194182A CN1194182A CN 97104939 CN97104939A CN1194182A CN 1194182 A CN1194182 A CN 1194182A CN 97104939 CN97104939 CN 97104939 CN 97104939 A CN97104939 A CN 97104939A CN 1194182 A CN1194182 A CN 1194182A
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Abstract
A fluid fuel reforming ceramic catalyst comprising a core of complex oxide ceramic of transition metals, an intermediate layer of an alumina-based silicate ceramic covering the core and an outer layer of a ceramic containing noble metals prepared by forming the core by firing the complex oxide ceramic of transition metals, coating the intermediate layer of the alumina-based silicate ceramic over the core, and coating the outer layer of the ceramic containing noble metals over the intermediate layer increases the octane number of fluid fuels, enhances their combustion efficiency, and decreases the noxious substances in exhaust gases.
Description
The present invention relates to improve effectively efficiency of combustion and pass through the fluid fuel reforming ceramic catalysts that reorganization reduces disagreeable material in gasoline, light oil and other liquid fuel and natural gas and other gaseous fuel.
For example gasoline also contains about 30% benzene, acetaldehyde and other incombustible and environmental pollutants except that containing about 60% inflammable substance, and contains about 10% raising octane number material, antifreezing agent and gaseous additives.Incombustible and environmental pollutants are discharged as material disagreeable in the waste gas owing to imperfect combustion.These incombustibles and environmental pollutants are reassembled as the ratio that inflammable substance can improve the inflammable substance that helps active combustion.Yet the supply (or air supply) that burning reorganization material must improve oxygen.Yet relatively large air contains relatively large nitrogen inevitably, increases the content of nitrogen oxide in the waste gas so inevitably.Although dissolve portion of air in the fuel, be not that the airborne oxygen of used dissolving all helps combustion reaction.If activate the oxygen of the dissolving that does not help combustion reaction, the extra inflammable substance that obtains by reorganization incombustible and environmental pollutants can burn effectively so, and need not to increase from the external world supply of air.
Therefore, the purpose of this invention is to provide airborne oxygen that the incombustible that will contain in the fluid fuel and environmental pollutants be reassembled as inflammable substance and be dissolved in fuel by activation with the catalyst that reduces disagreeable content of material in the waste gas and the manufacture method of this class catalyst.
In order to address the above problem, the invention provides:
(1) fluid fuel recombination catalyst, comprise transition metal compound oxidate ceramic core, cover core based on the silicate ceramics intermediate layer of aluminium oxide and the top ceramic layer that contains precious metal alloys that covers the intermediate layer,
(2) make the method for fluid fuel ceramic catalyst, comprise coating based on the silicate ceramics intermediate layer of aluminium oxide to cover transition metal compound oxidate ceramic core, coating contains the top ceramic layer of precious metal alloys.
Fig. 1 is the cutaway view that illustrates ceramic catalyst structure of the present invention.
The chromatogram of Fig. 2 for showing that the preceding light oil of impregnated catalyst is formed.
Fig. 3 is the chromatogram that light oil is formed behind the demonstration impregnated catalyst.
The electron spin resonance spectroscopy of Fig. 4 for showing that the oxygen base generates in the fuel.
Fig. 5 illustrates the relation between total aldehyde concentration in rotating speed of automobile engine and the waste gas.
Fig. 6 illustrates NO in automobile speed and the waste gas
xRelation between the concentration.
Fig. 7 illustrates the composition of burning gases in the engine cylinder and the relation between the rotating speed.
Fig. 8 illustrates the relation between catalyst consumption and the octane number.
Fig. 9 illustrates the relation between air-fuel ratio and the efficiency of combustion.
Following paragraph has been described fluid fuel reforming ceramic catalysts of the present invention. Fig. 1 is the figure explanation The cutaway view of bright fluid fuel reforming ceramic catalysts structure of the present invention. Fluid fuel reforming ceramic Catalyst 1 has three-decker basically, comprises transition metal compound oxidate ceramic core 2, cover (namely based on aluminium oxide) silicate ceramics that is basically formed by aluminium oxide of core 2 Intermediate layer 3 and the top ceramic layer that contains precious metal alloys 4 that covers intermediate layer 3.
Outer 4 and intermediate layer 3 formed by porous material, have the gas of permission by and allow The aperture of liquid turnover. Core 2 also is porous, although its porosity is greater than intermediate layer 3 Hes Outer 4, also allow gas to pass through and allows liquid to pass in and out. Border between each layer or Form the tilting structure that changes gradually, or the stepped construction of constitutive mutation. Should annotate Meaning arrives, and the variation of tilting structure potential energy is more continuous than stepped construction. This allows electronics to exist Successfully motion on the border allows oxidation-reduction reaction successfully to carry out, and strengthens by this intermediate layer With outer field regeneration efficiency. Therefore, the most handy tilting structure in each border.
Ceramic catalyst of the present invention generally is spherical substantially, also can make substantially post Shape.
Yet cylindrical catalyst can not keep containing core and intermediate layer and skin at its two ends Three-decker, all expose at its two ends. Comparatively speaking, be roughly spherical catalyst All keep in all directions three-decker, therefore preferably use to be substantially spherical catalysis Agent.
Ceramic catalyst of the present invention can use with liquid fuel such as gasoline, light oil and heavy oil and kerosene and the gaseous fuel such as town gas and propane.Ceramic catalyst of the present invention can directly place fuel, for example they is immersed in the fuel tank.
Core is made up of the transition metal compound oxidate ceramic, and it has the oxidation-reduction catalysis effect, and when Determination of Trace Sulfur, lead and other inorganic substances that contain in owing to pollution feul when outer and intermediate layer were lost its catalytic activity, core can make their regenerate.Electron motion in the core constitute is to intermediate layer and skin, and reduction is by the intermediate layer of catalyst poisoning contaminating impurity and outer field constitute.Because intermediate layer of polluting and therefore outer and detoxification, its catalytic activity is renewable.
The most handy MnO that contains of core
2, NiO, CoO and CuO the transition metal compound oxidate ceramic.Calculate by weight, core preferably contains 40-70 part MnO
2And the NiO of every kind of each 10-20 part, CoO and CuO.Above-mentioned four kinds of materials are critical.If any shortage in them or exceed above-mentioned scope does not then generate and has aperture and help the perovskite type crystal structure of oxidation-reduction electronics with storage, the result significantly reduces regeneration function.Catalyst of the present invention can contain other material, and effect has illeffects unless they are to redox catalysis.
The function in intermediate layer is that incombustible in the fuel and environmental pollutants are reassembled as inflammable substance.For example, the benzene that contains in the gasoline is because the phenyl ring bond fission, and described outer field catalytic action causes water decomposition and the hydrogen that produces carries out hydrogenation, is considered to be reassembled as methane, propane or other inflammable substance.Acetaldehyde is considered to be reassembled as methane, hydrogen and carbon dioxide by reacting with caused hydrogen ion and oxonium ion that water decomposition produces by outer catalytic action.
The intermediate layer is preferably by basically by aluminium oxide (promptly based on aluminium oxide) and silicate or preferably kaolin and the quartzy silicate ceramics of forming of carbon containing are formed.Calculate by weight, 70-90 part Al is preferably contained in the intermediate layer
2O
3With 10-30 part silicate, or preferably contain 5-10 part kaolin and 5-20 part carbon containing quartz.Al
2O
3Major function be carrier with silicate of catalytic action.Excessive Al
2O
3Reduce the silicate amount and the infringement catalytic action of carrying, and Al
2O
3Deficiency cause the reduction of mechanical strength.
Outer field function is to activate contained airborne oxygen in the fuel, emit by in the fuel moisture decomposition and the hydrogen and the newborn oxygen that produce.Thereby the inflammable substance that can burn increases by reorganization need not from the supply of external world's increase air.
Skin is preferably by containing Pt-Pd-Rh alloy and Al
2O
3Fire mixture, Mo-Al
2O
3Catalyst, La
0.5-Sr
0.5CoO
3Catalyst, be stated from Al
2O
3On vanadium oxide catalyst and/or Ag-Al
2O
3The precious metal alloys pottery that contains of catalyst is formed.
Be stated from Al
2O
3On vanadium oxide catalyst and Ag-Al
2O
3At least need one of them in the catalyst.
Calculate by weight, skin preferably contains Pt-Pd-Rh alloy and Al
2O
3Fire mixture, Mo-Al
2O
3Catalyst, La
0.5-Sr
0.5CoO
3Catalyst, be stated from Al
2O
3On vanadium oxide catalyst and/or Ag-Al
2O
3Catalyst, every kind contains 15-25 part.When components contents exceeds above-mentioned scope, be difficult to generate required pottery by firing, the result reduces the oxygen amount of activation and the water yield of decomposition.
The Pt-Pd-Rh alloy preferably contains Pt, Pd and the Rh of about 5-7: 1-3: 1-3 (weight ratio).Pt-Pd-Rh alloy and Al
2O
3Preferably mix with the ratio of about 4-5: 5-6 in advance.Al
2O
3Major function be carrier with Pt-Pd-Rh alloy of catalytic action.Al
2O
3The excessive silicate amount and the infringement catalytic action that can reduce carrying, and Al
2O
3Deficiency can cause the reduction of mechanical strength.Fire Pt-Pd-Rh alloy and Al at about 850-930 ℃
2O
3Mixture can prepare fires mixture.Mo-Al
2O
3Catalyst is with Al
2O
3Be the Mo catalyst of carrier, ratio is about 1: 1.La
0.5-Sr
0.5CoO
3Catalyst is the mixture of firing of lanthana, strontium oxide strontia and cobalt oxide.Be stated from Al
2O
3On vanadium oxide catalyst by about 9: 1 Al
2O
3Form with vanadium oxide.Ag-Al
2O
3Catalyst is with Al
2O
3Be the Ag catalyst of carrier, ratio is about 1Ag: 9 Al
2O
3
As what mention previously, the method of making ceramic catalyst of the present invention comprises fires transition metal compound oxidate ceramic core, outside core, be coated with silicate ceramics intermediate layer, and outside the intermediate layer, be coated with the top ceramic layer that contains noble metal based on aluminium oxide.Provide the method for making above-mentioned preferred ceramic catalyst below.
The catalyst that is used for core
MnO with required ratio
2, NiO, CoO and CuO mixture of powders and extra adhesive approximately 900-1000 ℃ fire, will fire product then and wear into powder.Make the pre-burned powder that obtains so for example that diameter is the ball of 1.5-2.0mm, with extra adhesive at about 1150-1350 ℃ of sintering.Sintering carries out in air.
The catalyst that is used for the intermediate layer
With the lanthana of required ratio and the silicate mixture such as kaolin and carbon containing quartz and extra adhesive approximately 1050-1200 ℃ fire, will fire product then and wear into powder.Add the pre-burned powder paste that adhesive and blowing agent (by emitting carbon dioxide or other gas makes the sintered product porous during sintering) preparation obtains like this.The paste that will obtain like this is coated on outside the core balls then, and its thickness is for example about 1mm.Catalyst that then will be by being coated with paste preparation outside core balls is at about 900-1100 ℃ of sintering.Sintering carries out in air.
When 900-1100 ℃ of sintering intermediate layer catalyst, the constitute of core and intermediate layer catalyst melts and counterdiffusion mutually.Thereby the border between core and intermediate layer forms the tilting structure that composition gradually changes.
Outer layer catalyst
The Pt-Pd-Rh alloy and the Al that prepare required ratio
2O
3Fire mixture, Mo-Al
2O
3Catalyst, La
0.5-Sr
0.5CoO
3Catalyst, be stated from Al
2O
3On vanadium oxide catalyst and/or Ag-Al
2O
3The mixture of powders of catalyst.Add adhesive and blowing agent mixture is made paste.The paste that will obtain like this is coated on firing outside the catalyst spheres of core and intermediate layer composition then, and its thickness is for example about 1mm.The product of firing coating in about 600-700 ℃ reducing atmosphere obtains ceramic catalyst of the present invention.With Pt-Pd-Rh alloy and Al
2O
3With required ratio mixture, and approximately 850-930 ℃ fire mixture, preparation Pt-Pd-Rh alloy and Al
2O
3Fire mixture.
When firing outer layer catalyst for 600-700 ℃, the constitute of skin and intermediate layer catalyst melts and counterdiffusion mutually.Thereby the border between skin and intermediate layer forms the tilting structure that composition gradually changes.
The stepped construction of component sudden change if desired so will be catalyst coated outside the core catalyst as the intermediate layer that the stickum of adhesive mixes with wax or other, omission sintering process subsequently.Equally, will be coated on outside the catalyst of intermediate layer, omit sintering process subsequently with the outer layer catalyst that identical stickum mixes.
In the manufacture process of ceramic catalyst of the present invention, core forms sphere substantially during sintering, uses intermediate layer and the skin that coating forms spherical substantially shell subsequently.Therefore, the whole ceramic catalyst of finishing is substantially sphere.
When in hydrostatic column, carrying out sintering, form columniform substantially core.Then, use coating subsequently and form the intermediate layer and the skin of columniform shell substantially.Therefore, the whole ceramic catalyst of finishing is substantially columniform.
Embodiment
Provide following examples so that detail of the present invention to be described.Embodiment only illustrates the present invention rather than in order to limit.
Embodiment described below is whole to be substantially spherically, and the border between each layer is to form the tilting structure that gradually changes.
The core catalyst
The adding of 58ml 7% (weight) polyvinyl alcohol water solution is contained 54g MnO
2, 15gNiO, 15g CoO and 16g CuO (all being powder type) mixture in.The mixture that obtains is like this fired at 950 ℃, will be fired product and wear into powder.With preparing paste in 30ml 7% (weight) the polyvinyl alcohol water solution adding pre-burned powder, paste is made the ball that diameter is approximately 2mm.1200 ℃ of sintered balls, obtain the core catalyst.
The intermediate layer catalyst
The adding of 40ml 7% (weight) polyvinyl alcohol water solution is contained in the 100g mixture of 85g aluminium oxide, 5g kaolin and 10g carbon containing quartz.The mixture that obtains is like this fired at 1150 ℃, will be fired product and wear into powder.To prepare paste in 30ml 7% (weight) polyvinyl alcohol water solution and 10ml12% (weight) the aqueous sodium carbonate adding pre-burned powder.The paste that obtains like this is coated on outside the spherical core catalyst, and thickness is approximately 1mm.At the ball of 900 ℃ of sinter coatings, obtain to contain the catalyst of the core that is coated with the intermediate layer.
Outer layer catalyst
The Pt-Pd-Rh alloy (ratio of the Pt that contains, Pd and Rh is 3: 1: 1) and the Al that will contain equivalent
2O
3Mixture fire at about 900 ℃.Then with the Pt-Pd-Rh alloy and the Al of equivalent
2O
3Fire mixture, Mo-Al
2O
3Catalyst (Mo that contains and Al
2O
3Ratio be 1: 1), carry Al
2O
3The vanadium oxide catalyst (Al that contains
2O
3With the ratio of vanadium oxide be 9: 1), Ag-Al
2O
3Catalyst (Ag that contains and Al
2O
3Ratio be 1: 9), La
0.5-Sr
0.5CoO
3Catalyst (gross weight 100g) mixes.Add 30ml 7% (weight) polyvinyl alcohol water solution and 10ml 12% (weight) aqueous sodium carbonate and prepare the mixture paste.The paste that obtains is coated on outside the spherical core, and thickness is approximately 1mm.Then the paste that obtains is coated on firing outside the catalyst spheres that core and intermediate layer form, its thickness is about 1mm.In carbon monoxide atmosphere, fire the coating ball at about 670 ℃ and obtain three layers of ceramic catalyst.
Ceramic catalyst with such acquisition carries out following test.
Incombustible is reassembled as inflammable substance
To drop in 1 liter of light oil by the 130mg catalyst spheres of above-mentioned preparation.Allow light oil place 1 hour, use gas chromatographic analysis then in room temperature.Use Hewlett-Packard ' s 5290 serial II chromatogram and alumina powder posts, carry out chromatography at 350 ℃.The chromatogram that before the catalyst spheres that shown Fig. 2 and Fig. 3 drops into and input back obtains.In Fig. 2 and Fig. 3, A
1And A
2Expression is based on the inflammable substance of methane, A
3Expression is based on the inflammable substance of ethane, ethene and acetylene, A
4Expression is based on the inflammable substance of propane and propylene.B represents pentane, and C represents butane, and D represents methylpentene, and E represents benzene.Can find out obviously that from chromatogram after catalyst of the present invention dropped into, the incombustible such as methylpentene and benzene reduced, and inflammable substance increases.
Be dissolved in the activation of the oxygen in the fuel
To drop in 1 liter of gasoline by the 130mg catalyst spheres of above-mentioned preparation.Allow gasoline place 1 hour in room temperature, electron spin resonance spectroscopy (ESR) (Fig. 4) has confirmed the generation of oxygen base in the gasoline.a
1-a
8Be decided to be the oxygen base.
The reduction of aldehyde concentration in the waste gas
About 8g is equipped with (capacity is 60 liters) in the petrolic fuel tanks of automobile of 1200cc by the catalyst spheres input of above-mentioned preparation, measures in engine speed and the waste gas relation between the aldehyde concentration always.Measure the absorption spectrum that obtains by spectrum analysis (by the infrared beamsplitter FTIR-2 that uses Shimazu Corp. to produce), determine its concentration.Fig. 5 has shown the input catalyst and has not dropped into result's (six mean value to get on the car) that catalyst obtains.As seen in fig. 5, the input of catalyst obviously reduces total aldehyde concentration, and irrelevant with engine speed.
The reduction of NOx concentration in the waste gas
About 8g is equipped with (capacity is 60 liters) in the petrolic fuel tanks of automobile of 1200cc by the catalyst spheres input of above-mentioned preparation, measures the relation between the NOx concentration in automobile speed and the waste gas.With its concentration of gas Chromatographic Determination.Fig. 6 has shown the input catalyst and has not dropped into the result that catalyst obtains.As seen in fig. 6, the input of catalyst obviously (approximately 29-33%) reduces NOx concentration in the waste gas, and irrelevant with the speed of a motor vehicle.Carry out differential thermal analysis by reducing about 7 ℃ of after drop into 271 ℃, measure pyrolysis temperature (burning-point) by 278 ℃ before the catalyst input.The reduction of this temperature is considered to suppress emitting of Nox.
The composition of burning gases in the cylinder
About 8g is equipped with (capacity is 60 liters) in the petrolic fuel tanks of automobile of 1200cc by the catalyst spheres input of above-mentioned preparation, with the composition of burning gases in the gas Chromatographic Determination engine cylinder.When in cylinder, firing and the back piston that explodes when getting back to the home position, get gas that 5ml discharges as sample.Obtain the seen in fig. 7 of result as showing, unreacted matters significantly is reduced to by about 15-21% before dropping into and drops into approximately 1.5-3.5% of back.After dropping into catalyst, the concentration of methane and acetylene also greatly reduces.
The relation of catalyst and octane number
It is in about 86 the regular price gasoline that the catalyst by above-mentioned preparation of difference amount is put into original octane number before the catalyst input, measures the variation of octane number.As Fig. 8 finding, the input of catalyst significantly improves octane number.Along with the increase of catalyst input amount (mg/l), octane number is linear substantially to be increased.
Relation with efficiency of combustion
In regular price gasoline, drop into the front and back of catalyst, measure petrolic efficiency of combustion with the ratio of every liter of 130mg.Drop into the efficiency of combustion before and after the catalyst in the regular price gasoline that Fig. 9 has shown.Under the condition of keeping constant fuel consumption, measure.As Fig. 9 finding, when air-fuel ratio was 16.7, the input of catalyst improved about 30% efficiency of combustion.
As discussed above, ceramic catalyst of the present invention is by being reassembled as incombustible in the fuel and environmental pollutants inflammable substance, activating oxygen contained in the fuel and emitting newborn oxygen by water contained in the decomposition fuel, strengthen the economy of fuel, and reduce the harmful substance in the waste gas.
Claims (12)
1. fluid fuel reforming ceramic catalysts, it comprises transition metal compound oxidate ceramic core, cover core based on the silicate ceramics intermediate layer of aluminium oxide and the top ceramic layer that contains precious metal alloys that covers the intermediate layer.
2. according to the fluid fuel reforming ceramic catalysts of claim 1, wherein core is mainly by containing MnO
2, NiO, CoO and CuO the transition metal composite oxides form, the intermediate layer is made up of the silicate ceramics based on aluminium oxide that contains aluminium oxide and silicate, skin comprises Pt-Pd-Rh alloy and Al by containing
2O
3On fire mixture, Mo-Al
2O
3Catalyst, La
0.5-Sr
0.5CoO
3Catalyst and be stated from Al
2O
3On vanadium oxide catalyst and/or Ag-Al
2O
3The pottery that contains precious metal alloys of catalyst is formed.
3. according to the fluid fuel reforming ceramic catalysts of claim 2, wherein core is by 40-70 part (weight) MnO
2And NiO, the CoO of every kind of each 10-20 part (weight) and CuO composition, the intermediate layer is made up of 70-90 part (weight) aluminium oxide and 10-30 part (weight) silicate, and is outer by 15-25 part (weight) Pt-Pd-Rh alloy and Al
2O
3The Mo-Al that fires mixture and every kind of each 15-25 part (weight)
2O
3Catalyst, La
0.5-Sr
0.5CoO
3Catalyst and be stated from Al
2O
3On vanadium oxide catalyst and/or Ag-Al
2O
3Catalyst is formed.
4. according to the fluid fuel reforming ceramic catalysts of claim 1, wherein core and intermediate layer and intermediate layer and outer field border have the tilting structure that the pottery composition gradually changes.
5. according to the fluid fuel reforming ceramic catalysts of claim 1, wherein core and intermediate layer and intermediate layer and outer field border have the stepped construction of ceramic constitutive mutation.
6. according to the fluid fuel reforming ceramic catalysts of claim 1, wherein core is roughly sphere, and intermediate layer and skin form spherical housing substantially.
7. according to the fluid fuel reforming ceramic catalysts of claim 1, wherein core is roughly cylindricality, and that intermediate layer and skin are roughly is cylindrical.
8. make the method for fluid fuel reforming ceramic catalysts, comprise the transition metal compound oxidate ceramic is fired the formation core, outside core, be coated with silicate ceramics intermediate layer based on aluminium oxide, and the step that outside the intermediate layer, is coated with the top ceramic layer that contains noble metal.
9. make the method for fluid fuel reforming ceramic catalysts, be included in the silicate ceramics intermediate layer of the outer coating of transition metal compound oxidate ceramic core, and outside the intermediate layer, be coated with the top ceramic layer that contains noble metal based on aluminium oxide.
10. make the method for fluid fuel reforming ceramic catalysts according to claim 8, wherein be coated with the intermediate layer of mixing and do not carry out sintering, the stepped construction with ceramic constitutive mutation is made on the border between core and intermediate layer and intermediate layer and the skin with skin with stickum.
11., wherein pass through with MnO according to the method for claim 8 manufacturing fluid fuel reforming ceramic catalysts
2, NiO, CoO and CuO mix with adhesive, fires mixture at 900-1000 ℃, will fire product and wear into powder, then with ground product with adhesive at 1150-1350 ℃ of sintering, form transition metal compound oxidate ceramic core; By aluminium oxide and silicate are mixed with adhesive, fire mixture at 1050-1200 ℃, to fire product and wear into powder, add adhesive and blowing agent ground product is made paste, paste is coated on outside the core, at 900-1100 ℃ of sinter coating layer, to form silicate ceramics intermediate layer based on aluminium oxide; By with Pt-Pd-Rh alloy and Al
2O
3Fire mixture, Mo-Al
2O
3Catalyst, La
0.5-Sr
0.5CoO
3Catalyst and be stated from Al
2O
3On vanadium oxide catalyst and Ag-Al
2O
3At least a mixing in the catalyst adds adhesive and blowing agent mixture is made paste, and paste is coated on the intermediate layer, fires coating layer at 600-700 ℃ in reducing atmosphere, forms the top ceramic layer that contains noble metal.
12. according to the method for claim 8 manufacturing fluid fuel reforming ceramic catalysts, wherein core is by 40-70 part (weight) MnO
2And NiO, the CoO of every kind of each 10-20 part (weight) and CuO composition, the intermediate layer is made up of 70-90 part (weight) aluminium oxide and 10-30 part (weight) silicate, and is outer by every kind of Pt-Pd-Rh alloy and Al that contains 15-25 part (weight)
2O
3Fire mixture, Mo-Al
2O
3Catalyst, La
0.5-Sr
0.5CoO
3Catalyst and be stated from Al
2O
3On vanadium oxide catalyst and/or Ag-Al
2O
3Catalyst is formed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97104939A CN1104956C (en) | 1997-03-25 | 1997-03-25 | Fluid fuel reforming ceramic catalysts and their manufacturing methods |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97104939A CN1104956C (en) | 1997-03-25 | 1997-03-25 | Fluid fuel reforming ceramic catalysts and their manufacturing methods |
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| Publication Number | Publication Date |
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| CN1194182A true CN1194182A (en) | 1998-09-30 |
| CN1104956C CN1104956C (en) | 2003-04-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN97104939A Expired - Fee Related CN1104956C (en) | 1997-03-25 | 1997-03-25 | Fluid fuel reforming ceramic catalysts and their manufacturing methods |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102287297A (en) * | 2010-06-18 | 2011-12-21 | 群山大学校产学协力团 | Fuel pre-treatment module for internal combustion engine |
| CN104099143A (en) * | 2013-04-11 | 2014-10-15 | 高天日 | Apparatus and method for manufacturing a reformed fuel |
| CN105478154A (en) * | 2015-12-14 | 2016-04-13 | 夏百庆 | Catalyst for high-activity fluidized bed |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2056424B (en) * | 1979-08-08 | 1983-07-06 | Johnson Matthey Co Ltd | Decomposition of ozone |
| JPS6388040A (en) * | 1986-09-30 | 1988-04-19 | Nippon Engeruharudo Kk | Catalyst for purifying exhaust gas for vehicle and its preparation |
| US5057483A (en) * | 1990-02-22 | 1991-10-15 | Engelhard Corporation | Catalyst composition containing segregated platinum and rhodium components |
| CN1060793A (en) * | 1990-10-22 | 1992-05-06 | 华东化工学院 | Multieffective non-noble metal catalyst |
-
1997
- 1997-03-25 CN CN97104939A patent/CN1104956C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102287297A (en) * | 2010-06-18 | 2011-12-21 | 群山大学校产学协力团 | Fuel pre-treatment module for internal combustion engine |
| CN102287297B (en) * | 2010-06-18 | 2013-11-20 | 群山大学校产学协力团 | Fuel pre-treatment module for internal combustion engine |
| CN104099143A (en) * | 2013-04-11 | 2014-10-15 | 高天日 | Apparatus and method for manufacturing a reformed fuel |
| CN105478154A (en) * | 2015-12-14 | 2016-04-13 | 夏百庆 | Catalyst for high-activity fluidized bed |
| CN105478154B (en) * | 2015-12-14 | 2019-09-03 | 中石化南京催化剂有限公司 | One kind being used for the agent of high activity fluid catalytic |
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| Publication number | Publication date |
|---|---|
| CN1104956C (en) | 2003-04-09 |
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