Low temperature SCR catalyst for denitrating diesel vehicle exhaust, and preparation method thereof

Abstract

Provided are a low-temperature SCR catalyst for denitrating diesel vehicle exhaust, and preparation method thereof. The catalyst uses a molecular sieve as a carrier, and uses metallic elements such as copper and iron as active components. The catalyst preparation method comprises: preprocessing the molecular sieve; conducting multiple equal-volume impreparations; after impreparation, drying to dehydrate, and calcining; and finally pulping and coating to prepare the catalyst. The catalyst employs base metals such as copper and iron instead of precious metals as active components, thus reducing costs, being harmless to humans, and being environmentally friendly. The preparation method of the catalyst is simple and feasible with low requirements for raw materials, employs a repeated but small-quantity method of equal volume impregnation; and enables active ions to be dispersed more uniformly as compared with the existing conventional preparation methods, thus improving utilization and improving low-temperature catalytic activity and durability.

Claims

1. A preparation method for a low-temperature selective catalytic reduction (SCR) catalyst for denitrating diesel vehicle exhaust, wherein the method comprises: preprocessing a ZSM-5, BEA or Y type molecular sieve by placing it in a ventilated oven, and heating the molecular sieve to 90 C. in the oven for 4 hours; conducting a first equal-volume impregnation by detecting a specific pore volume of the preprocessed molecular sieve, adding the preprocessed molecular sieve into a reaction kettle, preparing an aqueous solution of Cu.sup.2+ and Fe.sup.3+ to provide Cu.sup.2+ in an amount that is 1-2% of the total mass of the molecular sieve and Fe.sup.3+ in an amount that is 1.5-2.5% of the total mass of the molecular sieve, wherein a total amount of both Cu.sup.2+ and Fe.sup.3+ is in a proportion of 2.5-4.5% of a total mass of the molecular sieve, and a total volume of the aqueous solution=a mass of the molecular sieve*the specific pore volume, adding the solution in the form of mist spray, stirring the aqueous solution and the preprocessed molecular sieve together; then stirring and heating the aqueous solution and the preprocessed molecular sieve at a temperature of up to 80 C. until a fine powder is formed; drying to dehydrate the fine powder by calcining the fine powder in a ventilated oven at a temperature of 120 C., and passing the dried fine powder through a screen; repeating the first equal-volume impregnation; calcining the dried fine powder at a temperature of 550 C. and cooling it to room temperature to obtain a dark red powder; adding an adhesive to the dark red powder, coating a carrier with a fluid comprising the adhesive and the dark red powder, and heating, drying and calcining the fluid-coated carrier to prepare the catalyst.

2. A preparation method according to claim 1, wherein the soluble aqueous solution of Cu.sup.2+ and Fe.sup.3+ comprises copper nitrate and iron nitrate.

3. A preparation method according to claim 1, wherein the molecular sieve is heated at a temperature of 90 C. during preprocessing.

4. A preparation method according to claim 3, wherein the molecular sieve is heated in the oven for four hours during preprocessing, and preprocessing further comprises decreasing the temperature to room temperature after heating.

5. A preparation method according to claim 1, wherein, in the first equal-volume impregnation Cu.sup.2+ accounts for 1-2% of the total mass of the molecular sieve and Fe.sup.3+ accounts for 1.5-2.5% of the total mass of the molecular sieve.

6. A preparation method according to claim 1, wherein the first equal-volume impregnation comprises adding the aqueous solution in the form of mist spray to the preprocessed molecular sieve, prior to stirring the aqueous solution and the preprocessed molecular sieve.

7. A preparation method according to claim 6, wherein the aqueous solution and the preprocessed molecular sieve are stirred at a temperature of 60-80 C. for at least one hour.

8. A preparation method according to claim 1, wherein drying the fine powder comprises heating the fine powder in the ventilated oven at a temperature of 120 C. for two hours.

9. A preparation method according to claim 1, wherein the screen comprises a 40-mesh screen.

10. A preparation method according to claim 1, wherein the fluid-coated carrier is dried and calcined at a temperature of 550 C. for two hours.

11. A preparation method according to claim 1, wherein the fluid-coated carrier is heated at a temperature of up to 550 C. to prepare the catalyst.

12. A preparation method according to claim 1, wherein the fluid-coated carrier is calcined at 300 C. for 1 hour, then at 550 C., to prepare the catalyst.

13. A preparation method according to claim 1, wherein the Cu.sup.2+ is present in an amount of 2-4% of the total mass of the molecular sieve in the catalyst, and the Fe.sup.3+ is present in an amount of 3-5% of the total mass of the molecular sieve in the catalyst.

14. A preparation method according to claim 13, wherein the Cu.sup.2+ is present as 3% of the total mass of the molecular sieve in the catalyst, and the Fe.sup.3+ is present as 4% of the total mass of the molecular sieve in the catalyst.

15. A preparation method according to claim 1, e carrier comprises a ceramic or metal.

16. A preparation method according to claim 15, wherein the carrier has a honeycomb structure.

17. A preparation according to claim 15, wherein the carrier comprises cordierite.

18. A preparation method according to claim 1, wherein drying to dehydrate the fine powder comprises calcining the fine powder in the ventilated oven at 120 C. for two hours.

19. A preparation method according to claim 1, wherein calcining the dried fine powder comprises heating the dried fine powder at 550 C. for two hours and cooling it to room temperature to obtain the dark red powder.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is conversion performance curves of NO.sub.X of SCR catalyst at high sulfur environment of the present invention;

(2) FIG. 2 is conversion performance curves of NO.sub.X of SCR catalyst at different airspeeds of the invention;

(3) FIG. 3 is conversion performance curves of NO.sub.X of SCR catalyst at different hydrothermal aging conditions of the invention;

(4) FIG. 4 is emission value (g/kwh) of NO.sub.X of an SCR catalytic converter before and after a steady-state engine bench test of the invention.

EMBODIMENTS OF THE INVENTION

(5) The invention is further described based on the following examples, the examples are only used for further describing the invention but do not limit the protection scope of the invention, the person skilled in the art can carry out non-essential improvements and adjustments according to the above contents, without departing from the protection scope of the invention.

Embodiment 1

The Preparation for a Low-Temperature SCR Catalyst

(6) Step {circle around (1)}: preprocessing the molecular sieve: weighing accurately a molecular sieve; placing it in an oven, ventilating and heating the oven for four hours under the temperature of 90 C., removing water adsorbed on the surface and other impurities, and decreasing the temperature to be room temperature. Embodiment 1 adopts a BEA-type molecular sieve or a Y-type molecular sieve.

(7) Step {circle around (2)}: conducting equal-volume impreparation for the first time: detecting the specific pore volume of the material dried in Step {circle around (1)}, adding the molecular sieve powder in Step {circle around (1)} into a reaction kettle, calculating soluble molysite solid and soluble nantokite solid according to Cu.sup.2+ and Fe.sup.3+ respectively: Cu.sup.2+ accounts for 1-2% of the total mass of the molecular sieve, and Fe.sup.3+ accounts for 1.5-2.5% of the total mass of the molecular sieve, both of Cu.sup.2+ and Fe.sup.3+ are calculated according to their total amount: preparing Cu.sup.2+ and Fe.sup.3+ into aqueous solution according to the proportion of 2.5-4.5% of the total mass of the molecular sieve, the total volume of the solution=the mass of the molecular sieve*specific pore volume, slowly adding the solution in the form of mist spray, stirring the solution constantly and continuing to stir the solution for one hour after the completion of the addition of the solution; then stirring the solution under the temperature of 60 C. for one hour, heating it to be the temperature of 80 C. and continuing to stirring it into fine powder;

(8) Step {circle around (3)}: drying to dehydrate: taking out the powder in Step {circle around (2)}, encasing it in a stainless steel disc, calcining it in a ventilated oven under the temperature of 120 C. for two hours, removing water absorbed in surface and passing it through a 40-mesh screen;

(9) Step {circle around (4)}: conducting equal-volume impreparation for the second time: adding the obtained molecular sieve in Step {circle around (3)} into the reaction kettle, and repeating the impreparation steps of Step {circle around (2)} and Step {circle around (3)};

(10) Step {circle around (5)}: calcining: calcining the powder obtained in Step {circle around (4)} under the temperature of 550 C. for two hours, naturally cooling it down to the room temperature and obtaining dark red powder;

(11) Step {circle around (6)}: pulping and coating: powder material is prepared into pulp with solid content of 40%-42%. The pulp is coated on cordierite ceramic carrier, placed into an electric oven blast, then put in a box-type resistance furnace after drying, and calcined by the order from room temperature to 300 C. (1 hr)^550 C. to obtain the low-temperature SCR catalyst.

Embodiment 2

The Preparation of a Low-Temperature SCR Catalyst by the Mass Ratio of Cu2+ and Fe3+ of 2:5

(12) Weighing accurately a molecular sieve of 200 g; placing it in an oven, ventilating and heating the oven for four hours under the temperature of 90 C., removing water adsorbed on the surface and other impurities, and decreasing the temperature to be room temperature. Detecting its specific pore volume, and placing it into a reaction kettle. Placing copper nitrate [Cu(NO.sub.3).sub.2.3H.sub.2O] of 7.56 g and iron nitrate [Fe(NO.sub.3).sub.3.9H.sub.2O] of 36.07 g in water of 103.85 ml, and stirring an obtained solution until they are dissolved. Slowly adding the solution in the molecular sieve, stirring the solution constantly and continuing to stir the solution for one hour after the completion of the addition of the solution. Taking out the powder, encasing in a stainless steel disc, calcining in a ventilated oven under the temperature of 120 C. for two hours, removing water absorbed in a surface and passing the powder through a 40-mesh screen. Adding the obtained powder into the reaction kettle, adding equal-amount solution again, spraying mist into the solution and drying the solution. calcining the obtained powder under the temperature of 550 C. for two hours and obtaining dark red powder; adding an adhesive into the dark red powder, and preparing it into serous fluid which is coated on cordierite ceramic honeycomb carrier with the screen number of 400 cell/in.sup.2 and the volume of 38.4 ml, and drying and calcining the carrier to obtain a low-temperature SCR catalyst.

Embodiment 3

The Preparation of a Low-Temperature SCR Catalyst by the Mass Ratio of Cu2+ and Fe3+ of 3:4

(13) Weighing accurately a molecular sieve of 200 g; placing it in an oven, ventilating and heating the oven four hours under the temperature of 90 C., removing water adsorbed on the surface and other impurities, and decreasing the temperature to be room temperature. Detecting its specific pore volume, and placing it into a reaction kettle. Placing copper nitrate [Cu(NO.sub.3).sub.2.3H.sub.2O] of 11.34 g and iron nitrate [Fe(NO.sub.3).sub.3.9H.sub.2O] of 28.86 g in water of 105.89 ml, and stirring an obtained solution until they are dissolved. Other operation is the same as that of Embodiment 2.

Embodiment 4

The Preparation of a Low-Temperature SCR Catalyst by the Mass Ratio of Cu2+ and Fe3+ of 4:3

(14) Weighing accurately a molecular sieve of 200 g; placing it in an oven, ventilating and heating the oven four hours under the temperature of 90 C., removing water adsorbed on the surface and other impurities, and decreasing the temperature to be room temperature. Detecting its specific pore volume, and placing it into a reaction kettle. Placing copper nitrate [Cu(NO.sub.3).sub.2.3H.sub.2O] of 15.13 g and iron nitrate [Fe(NO.sub.3).sub.3.9H.sub.2O] of 21.64 g in water of 107.93 ml, and stirring an obtained solution until they are dissolved. Other operation is the same as that of Embodiment 2.

Comparative Example 1

(15) A conventional VTiW-type SCR catalyst sold on the market is dissected, and the catalyst, of which the specification of the carrier is the same as that of Embodiment 1, is selected.

(16) Detection Results

(17) The activity evaluation test of catalysts from the above embodiments and Comparative Example 1 is carried out. The test conditions are as follows:

(18) The volume composition of gases: nitric oxide: 500 ppm, ammonia: 500 ppm, carbon dioxide: 5%, vapour: 4.5%, oxygen: 14%, nitrogen: balance gas; airspeed: ^ h^.

(19) The evaluation results of activity are in the following Table 1.

(20) TABLE-US-00001 NO.sub.X T.sub.50/ C. T.sub.90/ C. Embodiment 2 165 210-568 Embodiment 3 157 196-565 Embodiment 4 150 192-530 Comparative Example 1 214 255-452

(21) The above table 1 shows the followings:

(22) The three kinds of catalysts have sound conversion temperature of NO.sub.X meeting the purification requirement for the current diesel vehicle exhaust.

(23) Comparing with Comparative Example, Embodiment 2, Embodiment 3 and Embodiment 4 all have lower ignition temperature and a larger conversion temperature window. Comparing with the conventional VTiW type SCR catalyst, the description of the low temperature SCR catalyst of the invention has better catalytic performance.

(24) Comparing with Example 2 and Example 4, Example 3 has lower ignition temperature of NO.sub.X and the maximum conversion temperature window, showing that the catalytic performance of the catalyst of Example 3 has the most catalytic performance.

Embodiment 5

The Performance Detection Experiment for Catalyst

(25) Related detection experiments are carried out for the catalyst prepared according to Embodiment 3. The results of sulfur resistance test, different airspeed tests, hydrothermal aging test and bench test show that the catalyst prepared according to this invention has excellent low-temperature ignition activity for NO.sub.X and the stability under the conditions of high sulfur, high airspeed and high temperatures.

(26) FIG. 1 is conversion performance curves of NO.sub.X of SCR catalyst at high sulfur environment of the present invention. FIG. 1 shows that the performance of the present catalyst is not substantially decreased after the aging under the conditions of 200 ppm SO.sub.2, 200 C. 29 hr (equivalent to the conditions that a vehicle runs 25,000 km with the fuel with sulfur content of 670 ppm). The catalyst still has very effective performance after the aging under the conditions of 600 ppm SO.sub.2, 200 C. 29 hr (equivalent to the conditions that a vehicle runs 25,000 km with the fuel with sulfur content of 2000 ppm). However, the sulfur content of the fuel of the present diesel vehicle is 350 ppm, therefore, the present catalyst has better sulfur resistance. The results are shown in the following table 2.

(27) TABLE-US-00002 NO.sub.X T.sub.50/ C. T.sub.90/ C. Fresh 157 196-565 After the aging under the conditions of 158 198-558 200 ppm SO.sub.2, 200 C. 29 hr After the aging under the conditions of 176 230-492 600 ppm SO.sub.2, 200 C. 29 hr

(28) FIG. 2 is conversion performance curves of NO.sub.X of SCR catalyst at different airspeeds of the invention. FIG. 2 shows that the conversion performance of NO.sub.X of the present catalyst is slightly decreased with the increase of airspeed but the decrease is not obvious, the present catalyst still has very effective performance under the conditions of 110,000 h.sup.1 airspeed. Therefore, the present catalyst has very sound airspeed performance. The results are shown in Table 3.

(29) TABLE-US-00003 NO.sub.X T.sub.50/ C. T.sub.90/ C. 40000 h.sup.1 165 194-519 60000 h.sup.1 168 202-529 80000 h.sup.1 172 226-534 110000 h.sup.1 177 253-542

(30) FIG. 3 is conversion performance curves of NO.sub.X of an SCR catalyst at different hydrothermal aging conditions of the invention. The table shows that the performance of the present catalyst is not obviously decreased after its aging under the conditions of 550 C. 75 hr and 600 C. 50 hr of the conventional VTiW type SCR catalyst; the present catalyst still has very effective performance after the aging under the worse high-temperature conditions of 670 C. 64 hr. Therefore, the present catalyst has very sound anti-hydrothermal aging performance. The results are shown in Table 4.

(31) TABLE-US-00004 NO.sub.X T.sub.50/ C. T.sub.90/ C. Fresh 157 196-565 After the aging under the 168 216-563 conditions of 550 C. 75 hrs After the aging under the 171 239-574 conditions of 600 C. 50 hrs After the aging under the 172 244->555 conditions of 670 C. 64 hrs

(32) FIG. 4 is emission value (g/kwh) of NO.sub.X of an SCR catalyst before and after a steady-state engine bench test of the invention. FIG. 4 shows that the average emission value of NO.sub.X is 2.8 g/kwh, which reaches the national IV standard after an SCR catalytic converter of the present invention is installed. (Engine Model: WP7, 4.2 L, national IV standard of 3.5 g/kwh. A bench test is carried out according to the procedures prescribed in national IV standard.).

(33) The above results show that: comparing with the conventional VTiW type SCR catalyst, the catalyst of the invention has better catalytic performance.