CN1018984B - Catalyzer for waste gas purification of copper, lanthanum-bearing oxidate and its producing method - Google Patents
Catalyzer for waste gas purification of copper, lanthanum-bearing oxidate and its producing methodInfo
- Publication number
- CN1018984B CN1018984B CN 89103448 CN89103448A CN1018984B CN 1018984 B CN1018984 B CN 1018984B CN 89103448 CN89103448 CN 89103448 CN 89103448 A CN89103448 A CN 89103448A CN 1018984 B CN1018984 B CN 1018984B
- Authority
- CN
- China
- Prior art keywords
- coating
- component
- active component
- catalytic active
- preparation
- 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.)
- Expired
Links
Landscapes
- Catalysts (AREA)
Abstract
The present invention relates to a supported catalyst which simultaneously has the activity of oxidating CO and HC and reducing NOx and belongs to the field of environment protection and catalytic purification. The catalyst does not use or only uses Pt, a kind of trace noble metal, as an active catalytic component, but takes rich transition metal oxides and rare earth compounds, such as CuO and La2O3, as a basic recipe. Catalysts which have the advantages of low cost, good activity in oxidation and reduction and high stability in using lead-contained gasoline are obtained by improving the preparation method, and can be conveniently used for purifying automobile exhaust or industrial waste gas and the waste gas of combustion furnaces for civil use.
Description
The present invention relates to the attached catalyst of a kind of CO of having, HC oxidation and NOx reducing activity, belong to environmental protection catalytic purification field.
In industrial waste gas, civilian combustion furnace waste gas and the vehicle exhaust; component to atmosphere pollution has carbon monoxide (CO), nitrogen oxide (NOx) and does not burn hydrocarbon compound (HC) etc. completely; how eliminating this class harmful substance, is one of research topic the most popular in the world today thereby purify air, protect environment, maintaining ecological balance.Closely during the last ten years, a large amount of foreign patents have been reported the ternary form catalyst that is used for purifying vehicle exhaust, can eliminate harmful substances such as CO, HC and NOx preferably.For example, EP142858, EP142859, DE3436400, day disclosure J6129355, and Japanese J61046247; J61129030 etc., but these catalyst all serve as that main some transition metal oxide etc. of adding is main active ingredient with noble metal or with the noble metal, not only cost height, and anti-lead poisoning ability.At present, also having not contain or only contain minute amount of noble metal, is the catalyst of main composition with transition metal oxide as catalytic activity with the composite metal oxide that contains rare earth, as DD242183, DE3642018, DE3606335, CN86105768, CN86103200, CN85109694, CN851022282 etc., but disclosed this class catalyst, mostly have CO, HC oxidation activity, not obvious to the reducing activity of NOx.
The object of the present invention is to provide a kind of with transition metal oxide CuO and La
2O
3Be the attached catalyst of main catalytic active component, it has CO, HC oxidation and the catalytic action of NOx reducing activity simultaneously, and to using doped fuel that high stability is arranged.
Purpose of the present invention realizes in the following manner:
Described catalyst is by with γ-Al
2O
3The carrier and the catalytic active component that are main composition constitute, and catalytic active component accounts for γ-Al
2O
3Carrier or γ-Al
2O
3The 10-30wt% of coating, its carrier can be granular, also can impose γ-Al on cellular matrix
2O
3Coating gets honeycomb support.The preparation method of pelleted substrate after all main batchings are added that an amount of distilled water mixes, forms through extrusion pelletizing, shaping, drying, roasting, and said main batching is to intend the thin dried glue (Al of water aluminium
2O
3.3H
2O), ceria (CeO
2) and talcum powder, wherein, ceria, talcum powder account for the 3-10wt% that intends the thin dried glue of water aluminium respectively, and 3-8wt%.Cordierite or alloy cellular matrix can be made of prior art, impose γ-Al with infusion process then
2O
3Coating.Its preparation method is: with the main batching of above-mentioned said carrier and distilled water, ethanol, rare HNO
3Mix, put into the ball mill ball milling 5-6 hour, form glue, again with the excess volume dip-coating on the honeycomb substrate that is evacuated, make coating weight account for the 10-20% of whole honeycomb substrate weight, component in the glue can be definite like this: adding distil water 1200-5000ml in every 1000g master's batching, 95% alcohol (C
2H
5OH) 1000-4000ml, 10% nitric acid (HNO
3) 300-1500ml.Described catalytic active component is with CuO(first component) and La
2O
3(second component) is basic recipe, wherein the gram atom of Cu/La is than being 0.5/1-1/1, in order to improve the oxidation activity of NOx reducing activity and CO, HC, can in basic recipe, add the 3rd component, it can be the oxide of V, Co, Ni, Fe, Cu/V wherein, Cu/Co, Cu/Ni, the gram atom ratio of Cu/Fe is respectively 5/1-1/1, the 4th component Pt that also can add trace in basic recipe is to improve low-temperature oxidation activity.Its content is the 0.005-0.01% of total catalyst weight.
The appendix method and the operation sequence of catalytic active component are:
(1) prepares the nitrate mixed solution that contains catalytic active component in proportion;
(2) with the pelleted substrate that is evacuated or have γ-Al
2O
3The coating honeycomb support immersed in the above-mentioned solution of equivalent or excess volume 10-60 minute;
(3) take out oven dry, and 350 ℃-450 ℃ constant temperature 2-3 hour;
(4) at 750-850 ℃ of roasting 2-6 hour;
(5) can immerse once more and contain in the Pt solution, take out after 3-5 minute, 120 ℃ of oven dry 2 hours;
(6) at 400-450 ℃ of logical H
2Gas 2-5 hour.
Said procedure (6) is a very important production link, and whether the catalyst that table 1 and table 2 have been listed same composition passes through H
2The performance comparison situation that reduction is handled, table 1 has provided CO+O
2In the reaction, the delta data of the reaction temperature when the CO conversion ratio is identical, table 2 have provided among the NO+CO, when the NO conversion ratio is identical, and the delta data of reaction temperature.In table 1, the table 2, A is without H
2The Comparative Examples of air-flow reduction, B is through H
2The embodiment of gas reduction.From two the table as can be seen, through H
2This catalyst that the air-flow reduction was handled, initiation temperature obviously lowers, and its oxidation and reproducibility improve greatly, and especially the raising of NOx reducing activity is more remarkable.
Table 1 CO+O
2CO conversion ratio (%)-reaction temperature in the reaction (℃)
CO conversion ratio (%) 20 50 80 100 remarks
Reaction temperature (℃)
Classification
Comparative example A 272 307 334 363 catalyst 200mg
Reaction gas component: CO:0.49%
O
2：5.2%
All the other are N for Embodiment B 160 174 184 202
2
Air speed: 4500 hours
-1
NO conversion ratio (%)-reaction temperature in the table 2 NO+CO reaction (℃)
NO conversion ratio (%) 20 50 80 100 remarks
Reaction temperature (℃)
Classification
Comparative example A 312 390 520 550 catalyst 400mg
Reaction gas component: CO:1.10%
NO：0.54%
All the other are N for Embodiment B 235 272 305 330
2
Air speed: 4500 hours
-1
The comparative example A:
(1) gets 30-60 order γ-Al
2O
3Be main pelleted substrate 42.5g, wherein contain ceria (CeO
2) and each 2g of talcum powder.
(2) weigh lanthanum nitrate La(NO
3)
22H
2O 10.90g;
Copper nitrate Cu(NO
3)
23H
2O 5.10g;
Nickel nitrate Ni(NO
3)
26H
2O 2.609;
With adding water after above-mentioned three kinds of nitrate mixing, make the 35ml nitrate mixed solution;
(3) above-mentioned pelleted substrate is immersed in the nitrate mixed liquor of equal-volume water absorption;
(4) after taking-up is shelved 0.5 hour, 120 ℃ of bakings 2 hours, be warming up to 350 ℃ with 10 ℃/component velocity again, constant temperature 2 hours is warming up to 800 ℃ with 20 ℃/component velocity, constant temperature 3 hours.
Embodiment B:
It is (1) .(4 .(3 .(2))) identical with the comparative example A,
(5) at 400 ℃ of pure hydrogen (H
2) constant temperature 2 hours in the air-flow.
Two embodiment are provided below again:
Embodiment C:
(1) gets one of cordierite honeycomb substrate (φ 125mm, long 85mm, 300 holes/inch
2);
(2) join the coating glue: intend thin water dry glue powder (Al
2O
33H
2O, 200 orders) 180g, CeO
29g, talcum powder 9g, distilled water 1000ml, ethanol (C
2H
5OH, 95%) 800ml, nitric acid (10%) 250ml are blended in the ball mill ball milling 5-6 hour;
(3) the cordierite honeycomb substrate is vacuumized the back and immerse constantly vibration taking-up after 5 minutes in the above-mentioned glue, dry up,, be warming up to 800 ℃ with 20 ℃/component velocity, constant temperature 3 hours 120 ℃ of bakings 2 hours;
(4) take by weighing 966.2g copper nitrate [Cu(NO
3)
23H
2O] and 1443.7g lanthanum nitrate [La(NO
3)
32H
2O] dissolving is made into the 2L aqueous solution;
(5) honeycomb substrate of gluing solution immerses in the above-mentioned solution of excess volume under vacuum condition;
(6) taking-up was shelved 12 hours, 120 ℃ of bakings 2 hours, was warming up to 400 ℃ with 10 ℃/component velocity, and constant temperature 2 hours is warming up to 800 ℃ with 20 ℃/component velocity again, constant temperature 3 hours;
(7) take by weighing platinum (Pt) 200mg,, become 1L solution with distilled water diluting after removing nitrate anion with a small amount of chloroazotic acid heating for dissolving;
(8) will immerse in (7) solution through the semi-finished product of (6) operation, take out after 3-5 minute;
(9) at 400 ℃ of pure hydrogen (H
2) constant temperature 3 hours in the air-flow, finished product.
Embodiment D:
(1) same Embodiment C .(3 .(2))
(4) take by weighing: 676.3g copper nitrate [Cu(NO
3)
23H
2O], 1443.7g lanthanum nitrate [La(NO
3)
32H
2O] and 484.6g ferric nitrate [Fe(NO
3)
39H
2O] dissolving is made into the 2L aqueous solution.
(5) same Embodiment C .(6);
(7) at 400 ℃ of hydrogen (H
2) constant temperature 3 hours in the air-flow, finished product.
To be assembled into catalytic cleaner respectively by each four of the catalyst of Embodiment C and D preparation, be installed in the position of the former silencer of China east wind EQ6100-I h type engine h, measure CO, HC and NOx conversion ratio under the idling.(this engine is distance travelled 96183km, uses No. 70 doped fuel), the gained data are listed in table 3.
Table 3: the conversion ratio of CO, HC and NOx under the idling
(measuring under the condition that air-fuel ratio does not have to control)
Delivery temperature purifying rate (%)
Embodiment (℃)
CO HC NOx
C 360 91.0 63.5 50.7
D 315 85.8 57.7 50.0
By the above, the present invention need not or only use minute amount of noble metal Pt, and be raw material with low-cost transition metal oxide of aboundresources and rare earth compound, make have CO simultaneously, the catalyst of HC oxidation and NOx reducing activity, with low cost, catalytic activity is high, doped fuel there is advantages of higher stability, can be used for purifying vehicle exhaust more conveniently, also can be widely used in the purification of industrial waste gas and civilian combustion furnace waste gas.
Claims (8)
1, a kind of exhaust gas purifying catalyst that closes copper, lanthanum-oxides that contains, in order to handle industry and civilian waste gas and vehicle exhaust, it is by with γ-Al
2O
3Be the carrier and the catalytic active component formation of principal component, catalytic active component uses the infusion process appendix in graininess γ-Al
2O
3On the carrier, or the surface has γ-Al
2O
3On the honeycomb support of coating, catalytic active component point γ-Al
2O
310～30wt% of carrier, the preparation method of its pelleted substrate is:
After will leading an amount of distilled water mixing of batching adding, form through extrusion, shaping, oven dry, roasting,
γ-Al on the honeycomb support
2O
3The preparation method of coating is:
To lead being made into the coating glue, and use the vacuum impregnation technology dip-coating on cellular matrix,
The appendix method of catalytic active component is:
(1) prepares the nitrate aqueous solution that contains catalytic active component in proportion;
(2) under vacuum condition, pelleted substrate or honeycomb support with coating are immersed in the above-mentioned nitrate solution of equivalent volumes or excess volume 10～60 minutes;
(3) take out oven dry and in 350 ℃～450 ℃ constant temperature 2 hours;
(4) 750 ℃～850 ℃ high-temperature roastings 2～6 hours;
(5) can immerse once more in platiniferous (Pt) solution, take out after 3～5 minutes 120 ℃ of oven dry 2 hours,
The invention is characterized in:
(a) the main batching of pelleted substrate or honeycomb support coating is: intend the thin dried glue of water aluminium
(Al
2O
33H
2O), ceria (CeO
2) and talcum powder, wherein ceria and talcum powder account for 3～10wt% and the 3～8wt% that intends the thin dried glue of water aluminium respectively;
(b) the coating glue on the honeycomb substrate is to be mixed by the alcohol of main batching, distilled water, 95% concentration and rare nitric acid to be incorporated in that ball milling formed in 5～6 hours on the ball mill, adding distil water 1200～5000ml in every 100g master's batching, 95%C
2H
5OH1000～4000ml, 10%HNO
3300～1500ml;
(c) include CuO (first component) and La in the prescription of catalytic active component
2O
3(second component), wherein the gram atom of Cu and La ratio is 0.5/1～1/1.
2, according to the catalyst of claim 1, it is characterized in that can adding the 3rd component in the prescription of described catalytic active component, it can select V, Co, Ni or Fe oxide respectively for use, Cu/V wherein, Cu/Co, Cu/Ni, the gram atom ratio of Cu/Fe is 5/1～1/1.
3, according to the catalyst of claim 1 or 2, it is characterized in that in the prescription of described catalytic active component, can add the 4th component Pt.Wherein Pt accounts for 0.005～0.01% of total catalyst weight.
4, preparation comprises preparation graininess γ-Al as the method for the exhaust gas catalyst of claim 1 cupric, lanthanum-oxides
2O
3Carrier or have γ-Al
2O
3The appendix method of the honeycomb support of coating and catalytic active component, the preparation method of its pelleted substrate is:
After will leading an amount of distilled water mixing of batching adding, form through extrusion pelletizing, shaping, oven dry, roasting;
γ-Al on the honeycomb support
2O
3The preparation method of coating is:
To lead being made into the coating glue, and use the vacuum impregnation technology dip-coating on cellular matrix;
The appendix method of catalytic active component is:
(1) prepares the nitrate aqueous solution that contains catalytic active component in proportion;
(2) under vacuum condition, pelleted substrate or honeycomb support with coating are immersed in the above-mentioned nitrate solution of equivalent volumes or excess volume 10～80 minutes;
(3) take out oven dry and in 350 ℃～450 ℃ constant temperature 2 hours;
(4) 750 ℃～850 ℃ high-temperature roastings 2～6 hours;
(5) can immerse once more in platiniferous (Pt) solution, take out after 3～5 minutes 120 ℃ of oven dry 2 hours,
The present invention is characterised in that:
(1) the main batching of described pelleted substrate or honeycomb support coating is to intend the thin dried glue (Al of water aluminium
2O
33H
2O), ceria (CeO
2) and talcum powder, wherein ceria and talcum powder account for the 3～10wt% that intends the thin dried glue of water aluminium respectively, 3～8wt%;
(2) γ-Al on the described cellular matrix
2O
3The coating glue is to prepare back ball milling on ball mill in proportion by the alcohol of main batching, distilled water, 95% concentration and rare nitric acid to form in 5～6 hours;
(3) appendix active component and the catalyst after 750 ℃～850 ℃ roastings are put into 400～450 ℃ of H again
2Reductase 12 in the air-flow environment～5 hour.
5,, it is characterized in that the configuration proportion of the coating glue of described honeycomb support is, adding distil water 1200～5000ml in every 1000g master's batching, 95% C according to the Preparation of catalysts method of claim 4
2H
5OH 1000～4000ml, 10%HNO
3300～1500ml.
6,, it is characterized in that including CuO(first component in the prescription of described catalytic active component according to the Preparation of catalysts method of claim 4) and La
2O
3(second component), wherein the gram atom of Cu and La ratio is 0.5/1～1/1.
7,, it is characterized in that to add the 3rd component in the prescription of described catalytic active component according to the Preparation of catalysts method of claim 4 or 6, it is the oxide of V, Co, Ni, Fe, Cu/V wherein, Cu/Co, Cu/Ni, the gram atom ratio of Cu/Fe is 5/1～1/1.
8,, it is characterized in that in the prescription of described catalyst activity component that can add the 4th component Pt, wherein pt accounts for 0.005～0.01% of catalyst total amount according to the Preparation of catalysts method of claim 4 or 6.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 89103448 CN1018984B (en) | 1989-05-17 | 1989-05-17 | Catalyzer for waste gas purification of copper, lanthanum-bearing oxidate and its producing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 89103448 CN1018984B (en) | 1989-05-17 | 1989-05-17 | Catalyzer for waste gas purification of copper, lanthanum-bearing oxidate and its producing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1047225A CN1047225A (en) | 1990-11-28 |
| CN1018984B true CN1018984B (en) | 1992-11-11 |
Family
ID=4855117
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 89103448 Expired CN1018984B (en) | 1989-05-17 | 1989-05-17 | Catalyzer for waste gas purification of copper, lanthanum-bearing oxidate and its producing method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1018984B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1057940C (en) * | 1996-07-17 | 2000-11-01 | 厦门大学 | Transition metal catalyst and its use method in preparing uniform-caliber nanometre carbon pipe |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1045549C (en) * | 1993-11-26 | 1999-10-13 | 中国科学技术大学 | Three-effect catalyst and preparing method containing copper and lanthanum-oxides, platinum and rhodium |
| CN1051025C (en) * | 1995-02-17 | 2000-04-05 | 段忠善 | Catalyst for purifying waste industrial gas and exhausted gas of automobile |
| CN1075400C (en) * | 1996-12-12 | 2001-11-28 | 北京科技大学 | Catalyst for purifying tail gas fro mautomobile by treating nitrogen oxides thereof |
| CN1047540C (en) * | 1997-10-31 | 1999-12-22 | 北京绿创环保科技有限责任公司 | Ternary composite metal oxide catalyst for treating automobile's waste gas, and method for preparing same |
| US20080120970A1 (en) * | 2006-11-29 | 2008-05-29 | Marcus Hilgendorff | NOx Storage Materials and Traps Resistant to Thermal Aging |
| CN102114426B (en) * | 2010-12-23 | 2012-11-21 | 内蒙古工业大学 | Special catalyst for cold hydrogenation of silicon tetrachloride and preparation method thereof |
| CN106492636A (en) * | 2016-11-24 | 2017-03-15 | 广东工业大学 | A kind of catalytic reduction method of NO and its application |
| CN108816224A (en) * | 2018-06-26 | 2018-11-16 | 中国天辰工程有限公司 | A kind of catalyst and preparation method handling the exhaust gas in the roasting of sial phosphorus molecular sieve |
-
1989
- 1989-05-17 CN CN 89103448 patent/CN1018984B/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1057940C (en) * | 1996-07-17 | 2000-11-01 | 厦门大学 | Transition metal catalyst and its use method in preparing uniform-caliber nanometre carbon pipe |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1047225A (en) | 1990-11-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1091002C (en) | Diesel catalytic converter | |
| CN1021412C (en) | Complex rare-earth oxidate containing valuable metal type honeycomb catalyst and its preparation | |
| CN1280010C (en) | Preparation method of metal honeycomb supported catalyst | |
| CN1572367A (en) | Method of preparing a double layered, palladium-only three-way catalyst | |
| CN113600188B (en) | Catalyst for purifying tail gas of gasoline car and preparation method thereof | |
| CN1101727C (en) | Rare earth-noble metal catalyst for purifying motor vehicle exhaust and its preparing method | |
| CN111215048A (en) | Ozone purification catalyst and preparation method and application thereof | |
| CN105772023A (en) | Manufacturing method for efficient three-component catalyst coating | |
| CN1018984B (en) | Catalyzer for waste gas purification of copper, lanthanum-bearing oxidate and its producing method | |
| CN1239258C (en) | Catalyst for purifying exhausted gas of car and preparation process thereof | |
| CN1128669C (en) | Automobile tail gas cleaning catalyst and its preparation method | |
| CN1045549C (en) | Three-effect catalyst and preparing method containing copper and lanthanum-oxides, platinum and rhodium | |
| JPH0714484B2 (en) | Nitrogen oxide reduction catalyst | |
| CN1036709A (en) | Vehicle exhaust gas systems | |
| CN1872409A (en) | Cleaning catalyst for tail gas of automobile, and preparation method | |
| CN1803263A (en) | Three-efficiency catalyst for purifying automobile end gas and its preparation method | |
| US20230256418A1 (en) | Three-way catalyst having low nh3 formation and preparation method therefor | |
| CN1824384A (en) | High performance low noble metal triple effect catalyst | |
| CN1272401A (en) | Automobile tail gas cleaning catalyst and its preparation method | |
| CN105498760B (en) | A kind of water resistant heat ageing method for preparing catalyst for natural gas and auto tail gas processing | |
| CN1072107A (en) | Rare-earth compound oxide type ternary catalyzer and preparation method | |
| US20070123418A1 (en) | Catalyst composition containing gallium for purifying exhaust gases of internal combustion engine | |
| CN110773159B (en) | Preparation process of Pt/Pd/Rh oxidation catalyst and catalyst prepared by same | |
| CN105688902B (en) | A kind of preparation method of new and effective cleaning catalyst for tail gases of automobiles | |
| CN1915489A (en) | Ternary Nano catalyst in use for cellular carrier of full metal, preparation method and coating process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C13 | Decision | ||
| GR02 | Examined patent application | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |