CN1087032A - Noble metal-rare-earth-transition metal catalyst for purifying waste gas and preparation thereof - Google Patents
Noble metal-rare-earth-transition metal catalyst for purifying waste gas and preparation thereof Download PDFInfo
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- CN1087032A CN1087032A CN 92113298 CN92113298A CN1087032A CN 1087032 A CN1087032 A CN 1087032A CN 92113298 CN92113298 CN 92113298 CN 92113298 A CN92113298 A CN 92113298A CN 1087032 A CN1087032 A CN 1087032A
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- transition metal
- rare earth
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Abstract
The invention belongs to a kind of exhaust gas purifying catalyst that contains noble metal-rare-earth-transition metal and preparation method thereof.
Noble metal active component of the present invention is Pt, at least a among the Pd, add rare earth elements such as La, Ce and transition metal Cu, Co, Ni in addition, catalyst carrier is Kunming Golden Horse china clay and yunnan polytechnic aluminium oxide, carrier adopts " water stacking method " to make ball-type, and active component takes the quick dipping of solution to be written into.This catalyst good purification, long service life, applied widely.
Description
The invention belongs to a kind of Catalysts and its preparation method that contains the waste gas purification of noble metal-rare-earth-transition metal.
It is a kind of cheap catalyst of setting about studying in nearly ten years that rare earth catalyst is used to purify automobile exhaust, but facts have proved, simple rare earth catalyst can not satisfy the strict demand of automobile purification, based on noble metal, rare earth is that the catalyst of assisting begins to use abroad, based on rare earth and transition metal, the catalyst that noble metal only accounts for trace is stepping up research, the patent report of this respect has US4274981, US4299734, US4410454, DE3010950, DE3223500, JP57～57175, FR2530489 etc., these patents almost relate to all rare earth elements and metal, its difference is a formula rate, preparation technology, and have nothing in common with each other in the properties of product aspect.
It is low and contain mixed catalyst of rare earth and transition metal and preparation method thereof that the present invention proposes a kind of bullion content.
Content of the present invention is:
1, noble metal active component is Pt, and is at least a among the Pd, and accounting for catalyst ratio is 0.01～0.09wt%, wherein Pt: Pd=7～9: 3～1.
2, rare earth element, the industrial dilute earth compounds that Gansu Rare Earth Co. provides provides with chloride or nitrate form, and calcination analysis composition (wt%) is after the hydrolysis: La
2O
328; CeO
240～45; Pr
6O
115～6; Al
2O
315～18; Heavy rare earth (mainly being Nd, Sm etc.) 1～2; Fe, Si surplus.The ratio that accounts in catalyst is 10～12wt%.
3, transition metal Co+Cu+Ni, wherein Cu: Co: Ni=1: 1: 1, the ratio that accounts in catalyst was 4～5wt%.
4, surplus is a catalyst carrier, and it consists of Kunming Golden Horse china clay and yunnan polytechnic aluminium oxide, and wherein the composition of Golden Horse china clay for (wt%) is: SiO
270～71; Al
2O
320～21; Fe
2O
30.4～0.5; CaO 0.8～0.9; MgO 0.4～0.5; TiO
20.03～0.04; Surplus is K
2O, Na
2O.
The composition of yunnan polytechnic aluminium oxide (wt%) is: Al
2O
395～98, all the other are CaO, MgO etc.
The ratio of Golden Horse china clay and commercial alumina is 3.5～5: 6.5～5.
5, manufacture craft may further comprise the steps:
(1) carrier preparation method
Adopt " water stacking method " in proportion the carrier powder of mixing (100 order) form about Φ 5mm the (bead of 4.7≤d≤4.8mm).
(2) rare earth and transition metal is written into
With rare-earth salts and transition metal salt (chloride or nitrate) weighing in proportion, water-soluble, hydrolysis under PH=7～8 conditions, filtration washing, oven dry, took exercise 2 hours for 500 ℃, rare earth and transition metal are the metal oxide form, take out after the cooling naturally to be milled down to≤100 orders are standby.
When catalyst carrier is molded into diameter and is about 5mm, stop to add the carrier powder, change and add rare earth and the transition metal oxide powder that has prepared, make carrier surface superscribe one deck rare earth and transition metal oxide with " water stacking method ", thickness is about 0.3～0.4mm.
(3) noble metal active component is written into:
With active noble metals component Pt, Pd makes corresponding chloro-complex (chloroplatinic acid, the acid of chlorine palladium) respectively and is mixed with the corresponding aqueous solution by required amount, adopt dipping (1 minute) fast then, quick-drying method makes noble metal component be fixed on carrier surface rapidly.
(4) with above-mentioned catalyst under 600 ℃ of temperature, H
2Reductase 12 hour in the atmosphere.
The advantage of catalyst of the present invention and method for making thereof is:
1, the support material of selecting for use is the commercial alumina in Kunming Golden Horse china clay and Yunnan, and the peculiar composition in the china clay can improve the low-temperature sintering performance and the working strength of carrier.
2, carrier adopts water stacking method to make sphere, can not only make the uniform ingredients of carrier, and preparation method is easy, and can make carrier have layer structure, and active component is stated from the top layer, the effect of favourable performance active component.
3, because the firing temperature of carrier is controlled to be 850～1170 ℃, and the aluminium oxide variant all is a～type in the carrier, and overall structure is the porous ceramics type, malleation intensity reaches 70～75Kg/cm
2, compare with external r～type or the r～P type mixed type variant that adopts usually, the intensity height of carrier, resistance to impact and high-temperature stability are stronger.
4, owing to adopt dipping fast, quick-drying method makes active component be fixed on carrier surface rapidly, and the 95% active constituent amount that reaches is distributed in and is no more than 0.2 millimeter surface, is beneficial to bring into play to greatest extent the effect of noble metal active component.
5, in catalyst, add rare earth element and transition metal, the cost of catalyst is descended, the anti-lead poisoning ability of catalyst is strengthened.
6, good purification, the CO clean-up effect reaches 90～98%, the clean-up effect 85～95% of CH.
7, catalyst long service life is used to surpass 1700～2000 hours in diesel engine (engineering machinery), using under doped fuel (lead tetraethide 1～2 grams per liter) the fuel situation, can keep purification efficiency, reaches service life more than 40,000 kilometers.
8, not only be suitable for automobile, the exhaust gas purification of diesel vehicle, and be applicable to loading, machineries such as mining transportation have extensive adaptability.
Embodiment one:
Take by weighing industrial rare earth-iron-boron 1.2Kg, Cu, Ni, Co nitrate in each 50 gram of metal, mixing is put into 5 liters of beakers, adds water and dissolves fully, the elimination insoluble matter.Heated solution adds NH to 80-85 ℃
4OH is hydrolyzed, precipitation finish (PH=8) filters afterwards, precipitation washes with water 3-5 time, 110 ℃ of down oven dry were calcined 2 hours under 500 ℃ and are obtained the oxide of rare earth and Cu, Ni, CO.Be milled down to≤100 orders, take by weighing 400 the gram standby.Golden Horse china clay and yunnan polytechnic aluminium oxide (4: 6) powder (≤100 order) are made the bead of diameter 4.7-4.8 millimeter with water stacking method.Weigh up 2800 grams (dry weight 2500 grams) after sieving and put into nodulizer.The rare earth that to get ready and Cu, Ni, CO oxide powder add gradually again, continue the balling-up operation, make above-mentioned oxide be wrapping to carrier surface, it is little 24 hours at indoor the moon to take out bead after oxide powder adds, oven dry (105 ℃) is 4 hours in the baking oven, calcined 5 hours down for 1110 ℃, the taking-up of cooling back is sieved and is obtained 5 millimeters beads of diameter, takes by weighing 300 grams and puts into beaker, restrains in 0.04% ratio platinum-impregnated 0.12 and (is made into H
2PtC
16Solution), rapid draing.600 ℃ of following H
2Reductase 12 hour promptly gets product.
Embodiment two
Take by weighing industrial rare earth nitrades 1.5Kg, Cu, Ni, CO nitrate in each 55 gram of metal.Put into 10 liters of ceramic cylinders, add water and dissolve elimination insoluble matter afterwards fully.Heated solution to 85 ℃-90 ℃ adds NH
4OH is hydrolyzed.Precipitate finish (PH=8) and leach sediment afterwards.With distilled water washing 3-5 time, take out that precipitation is put into that 500 ℃ of oven dry in the baking oven (110 ℃ 24 hours) were calcined 3 hours down and the oxide that obtains rare earth element and Cu, Ni, CO.Be milled down to≤100 orders, take by weighing 500 grams and expect standby.Use-case one described support material and method are made 4.7-4.8 millimeter bead, take by weighing 3700 grams (dry weight 3300 grams) carrier use-case one described method after sieving above-mentioned oxide is wrapping to carrier surface, indoor drying in the shade 24 hours, drying (105 ℃) is 4 hours in the baking oven, calcined 5 hours down for 1150 ℃, take out to sieve after the cooling and obtain 5 millimeters beads of diameter, take by weighing 300 gram beads and be written into platinum and palladium 0.03 gram and 0.045 gram, rapid draing, 600 ℃ of following H in 0.01% and 0.015% ratio with infusion process
2Reductase 12 hour gets product.
Claims (2)
1, a kind of exhaust gas purifying catalyst that contains noble metal, rare earth element and transition metal is characterized in that it consists of:
1, active component is Pt, and is at least a among the Pd, and the ratio that accounts in catalyst is 0.01～0.09wt%, wherein Pt: Pd=7～9: 3～1.
2, industrial dilute earth compounds (providing with chloride or nitrate form) is provided for rare earth element industrial goods, product, and producer is Gansu Rare Earth Co., and its composition (wt%) is: La
2O
328; CeO
240～45; Pr
6O
115～6; Al
2O
315～18; Heavy rare earth (mainly be rubidium, samarium, etc.) 1～2; Fe, Si surplus.The ratio that accounts in catalyst is counted 10～12wt% with oxide.
3, transition metal Co+Cu+Ni, wherein Cu: Co: Ni=1: 1: 1, the ratio that accounts in catalyst was 4～5wt%.
4, surplus is Kunming Golden Horse china clay and yunnan polytechnic alumina support, and wherein the composition of Kunming Golden Horse china clay (wt%) is: SiO
270～71; Al
2O
320～21; Fe
2O
30.4～0.5; CaO0.8～0.9; MgO0.4～0.5; TiO
20.03～0.04 all the other be K
2O, Na
2O.
The composition of yunnan polytechnic aluminium oxide (wt%) is: Al
2O
395～98, all the other are CaO, MgO etc.
The ratio of Golden Horse china clay and commercial alumina is 3.5～5: 6.5～5.
2, a kind of as the said Preparation of catalysts method of claim 1, it is characterized in that:
1, adopt " water stacking method " the carrier powder to be made the bead of 4.7≤d≤4.8mm.
2, with industrial dilute earth compounds and transition metal salt (both are chloride or nitrate form) weighing in proportion, water-soluble, hydrolysis under PH=7～8 conditions, filtration washing, oven dry, 500 ℃ of calcination 2 hours, rare earth and transition metal are oxide form, are milled down to≤100 orders after the cooling naturally.
3, continue to adopt water stacking method, rare earth and transition metal oxide powder wrapped are arrived original vector bead surface, the diameter of carrier beads is 5 ± 1mm.
4, under 850～1170 ℃ of temperature, the little ball forming of calcination.
5, noble metal active component is written into:
With precious metals pt, Pd makes corresponding chloro-complex respectively, is mixed with the corresponding aqueous solution by required amount, adopts dipping (1 minute) fast then, and quick-drying method makes noble metal component be fixed on carrier surface rapidly.
6, under 600 ℃ of temperature, H
2Calcination is 2 hours in the atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92113298 CN1032045C (en) | 1992-11-14 | 1992-11-14 | Noble metal-rare earth-transition metal catalyst for purifying waste gas and preparation thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92113298 CN1032045C (en) | 1992-11-14 | 1992-11-14 | Noble metal-rare earth-transition metal catalyst for purifying waste gas and preparation thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1087032A true CN1087032A (en) | 1994-05-25 |
| CN1032045C CN1032045C (en) | 1996-06-19 |
Family
ID=4946341
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 92113298 Expired - Fee Related CN1032045C (en) | 1992-11-14 | 1992-11-14 | Noble metal-rare earth-transition metal catalyst for purifying waste gas and preparation thereof |
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|---|---|
| CN (1) | CN1032045C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102039145A (en) * | 2009-10-20 | 2011-05-04 | 认知-普拉斯株式会社 | Catalyst for purifying discharging gas and method manufacturing the same |
| CN101309866B (en) * | 2005-09-08 | 2011-08-17 | 韩华石油化学株式会社 | Method for preparing precious metals oxide, oxygen storage material and catalyst system composed by precious metals oxide |
| CN105080567A (en) * | 2014-04-22 | 2015-11-25 | 中国科学院长春应用化学研究所 | Catalyst and aromatic amino compound preparation method |
| CN111111750A (en) * | 2019-12-25 | 2020-05-08 | 中国航空工业集团公司金城南京机电液压工程研究中心 | Catalyst for green inerting system of aircraft fuel tank and preparation method thereof |
-
1992
- 1992-11-14 CN CN 92113298 patent/CN1032045C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101309866B (en) * | 2005-09-08 | 2011-08-17 | 韩华石油化学株式会社 | Method for preparing precious metals oxide, oxygen storage material and catalyst system composed by precious metals oxide |
| CN102039145A (en) * | 2009-10-20 | 2011-05-04 | 认知-普拉斯株式会社 | Catalyst for purifying discharging gas and method manufacturing the same |
| CN105080567A (en) * | 2014-04-22 | 2015-11-25 | 中国科学院长春应用化学研究所 | Catalyst and aromatic amino compound preparation method |
| CN111111750A (en) * | 2019-12-25 | 2020-05-08 | 中国航空工业集团公司金城南京机电液压工程研究中心 | Catalyst for green inerting system of aircraft fuel tank and preparation method thereof |
| CN111111750B (en) * | 2019-12-25 | 2023-04-11 | 中国航空工业集团公司金城南京机电液压工程研究中心 | Catalyst for green inerting system of aircraft fuel tank and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1032045C (en) | 1996-06-19 |
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Free format text: CORRECT: PATENTEE; FROM: KUNMING INSTITUTE OF PRECIOUS METALS TO: GUIYAN PLATIUM CO., LTD. |
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| CP03 | Change of name, title or address |
Address after: Walnut, two ring road, Yunnan, Kunming Patentee after: Guiyan Platinum Industry Co., Ltd. Patentee before: Kunming Institute of Precious Metals |
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Owner name: YOU KUMING INQUIRY LIMITED LIABILITY CATALYST CO. Free format text: FORMER OWNER: GUIYAN PLATIUM CO., LTD. Effective date: 20020401 |
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Effective date of registration: 20020401 Address after: 650000 Kunming hi tech Industrial Development Zone, Yunnan, Lu Jun Patentee after: Guiyan Catalyst Co., Ltd., Kunming Address before: 650221, Yunnan Kunming Second Ring Road walnut head: Bullock Patentee before: Guiyan Platinum Industry Co., Ltd. |
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| C15 | Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993) | ||
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| C19 | Lapse of patent right due to non-payment of the annual fee | ||
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