Method for the Direct Synthesis of Cu-Containing Silicoaluminate Material with the AEI Zeolite Structure, and the Catalytic Applications Thereof

Abstract

The main object of the present invention is to provide a new method for preparing the copper-containing silicoaluminate form of the AEI zeolite structure by means of a direct synthesis methodology. This new process involves combining a organometallic copper-complex with an additional organic molecule capable of directing the crystallisation of the silicoaluminate form of the AEI zeolite structure as organic structure-directing agents (OSDAs).

Claims

1-36. (canceled)

37. Process for the direct synthesis of a material with the copper-containing silicoaluminate form of the AEI zeolite structure, which comprises, at least, the following steps: (i) Preparation of a mixture containing, at least, one source of water, one source of copper, one polyamine, selected from tetraethylenepentamine, triethylenetetramine, 1,4,8,11-tetraazacyclotetradecane, 1,4,8,11-tetramethyl-1,4,8,11-tetraazacyclotetradecane, or mixtures thereof, one source of tetravalent element Y, which is Si, and one source of trivalent element X, which is Al, one cyclic ammonium cation with alkyl substituents as the OSDA, selected from N,N-dimethyl-3,5-dimethylpiperidinium (DMDMP), N,N-diethyl-2,6-dimethylpiperidinium (DEDMP), N,N-dimethyl-2,6-dimethylpiperidinium, N-ethyl-N-methyl-2,6-dimethylpiperidinium, and combinations thereof, and one source of alkaline or alkaline-earth cations (A), comprising Na, where the synthesis mixture has the following molar composition: YO.sub.2: a X.sub.2O.sub.3: b OSDA: c A: d H.sub.2O: e Cu: f Polyamine where a ranges between 0.001 and 0.2; b ranges between 0.01 and 2; c ranges between 0.01 and 0.8; d ranges between 1 and 200; e ranges between 0.001 and 1; f ranges between 0.001 and 1; (ii) Crystallisation of the mixture obtained in (i) in a reactor, and (iii) Recovery of the crystalline material obtained in (ii).

38. Process for the direct synthesis of a material according to claim 37, wherein a zeolite with the FAU structure is the only source of Y and X.

39. Process for the direct synthesis of a material according to claim 37, wherein the source of alkaline or alkaline-earth cations (A) is selected from a source of Na, K, and combinations thereof.

40. Process for the direct synthesis of a material according to claim 37, wherein the source of copper is selected from nitrate, sulfate, and oxalate salts, and combinations thereof.

41. Process for the direct synthesis of a material according to claim 37, wherein the crystallisation process described in (ii) is performed at a temperature ranging between 100 C. and 200 C.

42. Process for the direct synthesis of a material according to claim 37, wherein the crystallisation time for the process described in (ii) ranges between 6 hours and 50 days.

43. Process for the direct synthesis of a material according to claim 37, further comprising the addition of AEI crystals, as seeds, to the synthesis mixture in a quantity of up to 25% by weight with respect to the total quantity of oxides.

44. Process for the direct synthesis of a material according to claim 37, wherein the recovery step (iii) is performed by means of a separation technique selected from decantation, filtration, ultrafiltration, centrifugation, and combinations thereof.

45. Process for the direct synthesis of a material according to claim 37, further comprising the elimination of the organic content retained inside the material by means of an extraction process.

46. Process for the direct synthesis of a material according to claim 37, further comprising the elimination of the organic content retained inside the material by means of a heat treatment at temperatures ranging between 100 C. and 1000 C., for a period of time ranging between 2 minutes and 25 hours.

47. Process for the direct synthesis of a material according to claim 37, wherein the material obtained is pelletised.

48. Process for the direct synthesis of a material according to claim 37, further comprising the introduction of at least one precious metal.

49. Process for the direct synthesis of a material according to claim 45, wherein the precious metal is selected from Pd, Pt, and combinations thereof.

50. Zeolite material with the AEI structure obtained according to the process of claim 37, wherein the zeolite material has the following molar composition after being calcined: YO.sub.2: o X.sub.2O.sub.3: pA: r Cu where o ranges between 0.001 and 0.2; where p ranges between 0 and 2; and where r ranges between 0.001 and 1.

51. Zeolite material with the AEI structure obtained according to claim 47, wherein the material is Cu-SSZ-39.

52. Zeolite material with the AEI structure obtained according to claim 47, further comprising a precious metal.

53. Zeolite material with the AEI structure obtained according to claim 49, wherein the precious metal is selected from Pd, Pt, and combinations thereof.

54. Method of using the zeolite material with the AEI structure described in claim 50, in processes for converting feeds formed by organic compounds into higher-value-added products, or for the elimination/separation of the reactive stream comprising the step of placing said feed in contact with the zeolite material.

55. Method of using the zeolite material with the AEI structure according to claim 51, wherein the zeolite material is a catalyst in the selective catalytic reduction (SCR) of nitrogen oxides (NOx) in a gas stream.

56. Method of using the zeolite material with the AEI structure according to claim 52, wherein the zeolite material is a catalyst in the SCR of NOx, which is performed in the presence of a reducing agent selected from ammonia, urea, hydrocarbons, and combinations thereof.

57. Method of using the zeolite material with the AEI structure according to claim 51, wherein the zeolite material is a catalyst in the conversion of methane into methanol.

58. Method of using the zeolite material with the AEI structure according to claim 50, wherein the zeolite material is a catalyst in the selective oxidation of ammonia to nitrogen.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0060] FIG. 1: PXRD patterns of the Cu-silicoaluminate materials with the AEI structure synthesised according to the present invention.

[0061] FIG. 2: UV-Vis spectrum of the Cu-silicoaluminate material with the AEI structure synthesised according to Example 2 of the present invention.

EXAMPLES

Example 1: Synthesis of N,N-dimethyl-3,5-dimethylpiperidinium (DMDMP)

[0062] 10 g of 3,5-dimethylpiperidine (Sigma-Aldrich, 96% by weight) is mixed with 19.51 g of potassium bicarbonate (KHCO.sub.3, Sigma-Aldrich; 99.7% by weight), and dissolved in 140 ml of methanol. Subsequently, 54 ml of methyl iodide (CH.sub.3I, Sigma-Aldrich, 99% by weight) is added, and the resulting mixture is kept under stirring for 5 days at room temperature. Once this time has elapsed, the reaction mixture is filtered in order to eliminate the potassium bicarbonate. The filtrated solution is partially concentrated by means of a rotary evaporator. Once the methanol has been partially evaporated, the solution is washed with chloroform several times and magnesium sulfate is added (MgSO.sub.4, Sigma-Aldrich, 99.5% by weight). Subsequently, the mixture is filtered in order to eliminate the magnesium sulfate. The ammonium salt is obtained by precipitation with diethyl ether and subsequent filtration. The final yield of N,N-dimethyl-3,5-dimethylpiperidinium iodide is 85%.

[0063] In order to prepare the hydroxide form of the preceding organic salt: 10.13 g of the organic salt is dissolved in 75.3 g of water. Subsequently, 37.6 g of an anion-exchange resin (Dower SBR) is added, and the resulting mixture is kept under stirring for 24 hours. Finally, the solution is filtered, to obtain N,N-dimethyl-3,5-dimethylpiperidinium hydroxide (with a 94% exchange).

Example 2: Direct Synthesis of the Cu-silicoaluminate With the AEI Structure

[0064] 154.0 mg of a 20% by weight aqueous solution of copper sulfate (II) (CuSO.sub.4, Alfa Aesar, 98%) is mixed with 31.2 mg of tetraethylenepentamine (TEPA, 98%, Sigma Aldrich), in order to prepare the organometallic copper-complex in situ, keeping the resulting mixture under stirring for 2 hours. Once this time has elapsed, 3216.0 mg of a 7.4% by weight aqueous solution of N,N-dimethyl-3,5-dimethylpiperidinium hydroxide and 163.1 mg of a 20% by weight aqueous solution of sodium hydroxide are added, keeping the resulting mixture under stirring for 15 minutes. Finally, 235.3 mg of a zeolite with the FAU structure (CBV-720, SiO.sub.2/Al.sub.2O.sub.3 molar ratio=21) is introduced into the synthesis mixture and kept under stirring for the period of time required to evaporate the excess water and achieve the desired gel concentration. The final composition of the gel is SiO.sub.2: 0.047 Al.sub.2O.sub.3: 0.046 Cu(TEPA).sup.2+: 0.2 DMDMP: 0.2 NaOH: 23 H.sub.2O. The resulting gel is transferred to a teflon-lined autoclave. The crystallisation is performed at 135 C. for 7 days under static conditions. The solid product is filtered, washed abundantly with water, dried at 100 C. and, finally, calcined in air at 550 C. for 4 h in order to eliminate the organic remainders. The yield of the solid obtained is greater than 90% (without taking the organic remainders into account).

[0065] The solid is characterised by means of powder X-ray diffraction, and the characteristic peaks of the AEI structure are obtained (see FIG. 1). Chemical analyses of the sample indicate a Si/Al ratio of 9.95 and a copper content of 3.3% by weight.

[0066] The uncalcined crystalline material obtained is characterised by UV-VIS spectroscopy in order to study the stability of the molecules of the organometallic copper-complex after the crystallisation of the zeolite. As can be observed in FIG. 2, the UV-VIS spectrum shows a single band centred at 265 nm, which has been assigned to the presence of the intact Cu-TEPA complex inside the zeolite structure (Franco, et al. 2013/159828, 2012).

Example 3: Direct Synthesis of the Cu-silicoaluminate With the AEI Structure

[0067] 75.1 mg of a 20% by weight aqueous solution of copper sulfate (II) (CuSO.sub.4, Alfa Aesar, 98%) is mixed with 18.0 mg of tetraethylenepentamine (TEPA, 98%, Sigma Aldrich), in order to prepare the organometallic copper-complex in situ, keeping the resulting mixture under stirring for 2 hours. Once this time has elapsed, 4049.0 mg of a 5.9% by weight aqueous solution of N,N-dimethyl-3,5-dimethylpiperidinium hydroxide and 159.1 mg of a 20% by weight aqueous solution of sodium hydroxide are added, keeping the resulting mixture under stirring for 15 minutes. Finally, 285.2 mg of a zeolite with the FAU structure (CBV-720, SiO.sub.2/Al.sub.2O.sub.3 molar ratio=21) is introduced into the synthesis mixture, and kept under stirring for the period of time required to evaporate the excess water and achieve the desired gel concentration. The final composition of the gel is SiO.sub.2: 0.047 Al.sub.2O.sub.3: 0.019 Cu(TEPA).sup.2+: 0.3 DMDMP: 0.2 NaOH: 18 H.sub.2O. The resulting gel is transferred to a teflon-lined autoclave. The crystallisation is performed at 135 C. for 7 days under static conditions. The solid product is filtered, washed abundantly with water, dried at 100 C. and, finally, calcined in air at 550 C. for 4 h in order to eliminate the organic remainders. The yield of the solid obtained is greater than 90% (without taking the organic remainders into account). The solid is characterised by means of powder X-ray diffraction, and the characteristic peaks of the AEI structure are obtained (see FIG. 1).

Example 4: Direct Synthesis of the Cu-silicoaluminate With the AEI Structure

[0068] 112.2 mg of a 20% by weight aqueous solution of copper sulfate (II) (CuSO.sub.4, Alfa Aesar, 98%) is mixed with 27.0 mg of tetraethylenepentamine (TEPA, 98%, Sigma Aldrich), in order to prepare the organometallic copper-complex in situ, keeping the resulting mixture under stirring for 2 hours. Once this time has elapsed, 2416.0 mg of a 7.4% by weight aqueous solution of N,N-dimethyl-3,5-dimethylpiperidinium hydroxide and 66.2 mg of a 20% by weight aqueous solution of sodium hydroxide are added, keeping the resulting mixture under stirring for 15 minutes. Finally, 196.2 mg of a zeolite with the FAU structure (CBV-720, SiO.sub.2/Al.sub.2O.sub.3 molar ratio=21) is introduced into the synthesis mixture, and kept under stirring for the period of time required to evaporate the excess water and achieve the desired gel concentration. The final composition of the gel is SiO.sub.2: 0.047 Al.sub.2O.sub.3 : 0.041 Cu(TEPA).sup.2+: 0.3 DMDMP: 0.1 NaOH: 21 H.sub.2O. The resulting gel is transferred to a teflon-lined autoclave. The crystallisation is performed at 135 C. for 7 days under static conditions. The solid product is filtered, washed abundantly with water, dried at 100 C. and, finally, calcined in air at 550 C. for 4 h in order to eliminate the organic remainders. The yield of the solid obtained is greater than 90% (without taking the organic remainders into account). The solid is characterised by means of powder X-ray diffraction, and the characteristic peaks of the AEI structure are obtained.

Example 5: Catalytic Assay of the SCR of NO.SUB.x

[0069] The catalytic activity for the selective catalytic reduction of NOx is studied using a quartz fixed-bed tubular reactor 1.2 cm in diameter and 20 cm in length. In a typical experiment, the catalyst is compacted into particles with a size ranging between 0.25-0.42 mm, which are introduced into the reactor, and the temperature is increased to 550 C. (see the reaction conditions in Table 1); subsequently, this temperature is maintained for one hour under a flow of nitrogen. Once the desired temperature has been reached, the reaction mixture is fed. The SCR of NOx is studied using NH.sub.3 as the reducing agent. The NOx present at the reactor gas outlet is continuously analysed by means of a chemiluminescence detector (Thermo 62C). The catalytic results are summarised in Table 2.

TABLE-US-00001 TABLE 1 Reaction conditions for the SCR of NOx. Total gas flow (ml/min) 300 Catalyst loading (mg) 40 NO concentration (ppm) 500 NH.sub.3 concentration (ppm) 530 O.sub.2 concentration (%) 7 H.sub.2O concentration (%) 5 Temperature interval studied ( C.) 170-550

TABLE-US-00002 TABLE 2 Conversion (%) of NOx at different temperatures (200, 250, 300, 350, 400, 450, 500) using the Cu-AEI catalyst synthesised following the methodology described in the present invention. Conversion (%) of NOx at different temperatures 200 C. 250 C. 300 C. 350 C. 400 C. 450 C. 500 C. Ex- 71.7 98.4 99.6 99.8 97.1 96.9 85.1 ample 2