Iron-loaded small pore aluminosilicate zeolites and method of making metal loaded small pore aluminosilicate zeolites

Abstract

The present invention provides an iron-loaded aluminosilicate zeolite having a maximum pore opening defined by eight tetrahedral atoms and having the framework type CHA, AEI, AFX, ERI or LTA, wherein the iron (Fe) is present in a range of from about 0.5 to about 5.0 wt. % based on the total weight of the iron-loaded aluminosilicate zeolite, wherein an ultraviolet-visible absorbance spectrum of the iron-loaded synthetic aluminosilicate zeolite comprises a band at approximately 280 nm, wherein a ratio of an integral, peak-fitted ultraviolet-visible absorbance signal measured in arbitrary units (a.u.) for the band at approximately 280 nm to an integral peak-fitted ultraviolet-visible absorbance signal measured in arbitrary units (a.u.) for a band at approximately 340 nm is >about 2. The present invention further provides a method of making an metal-loaded aluminosilicate zeolite having a maximum pore opening defined by eight tetrahedral atoms from pre-existing aluminosilicate zeolite crystallites, wherein the metal is present in a range of from 0.5 to 5.0 wt. % based on the total weight of the metal-loaded aluminosilicate zeolite.

Claims

1. An iron-loaded aluminosilicate zeolite-derived material having a maximum pore opening defined by eight tetrahedral atoms and having the framework type CHA, AEI, AFX, ERI, or LTA, obtained by a method comprising the steps of: (i) introducing mesoporosity into aluminosilicate zeolite crystallites by application of an aqueous alkali treatment to dissolve silica or application of an aqueous acidic treatment to dissolve alumina in the aluminosilicate zeolite crystallites; (ii) introducing the iron into the product of step (i) by wet impregnation or wet ion- exchange by contacting the product of step (i) with a mixture of an iron-containing reagent and a structure directing agent for the aluminosilicate zeolite; and (iii) closing the mesopores of the product of step (ii), thereby producing the iron-loaded aluminosilicate zeolite-derived material, wherein an ultraviolet-visible absorbance spectrum of the iron-loaded aluminosilicate zeolite-derived material comprises a band at approximately 280 nm, and, wherein a ratio of an integral, peak-fitted ultraviolet-visible absorbance signal measured in arbitrary units (a.u.) for the band at approximately 280 nm to an integral, peak-fitted ultraviolet-visible absorbance signal measured in arbitrary units (a.u.) for a band at approximately 340 nm is greater than about 2.

2. The iron-loaded aluminosilicate zeolite-derived material according to claim 1, wherein a ratio of an integral ultraviolet-visible absorbance signal measured in arbitrary units (a.u.) for the band at approximately 280 nm to an integral ultraviolet-visible absorbance signal measured in arbitrary units (a.u.) for a band at approximately 470 nm is >5.

3. The iron-loaded aluminosilicate zeolite-derived material according to claim 1, wherein the iron is present in the range of from about 0.7 to about 3.0 wt. % based on the total weight of the iron-loaded aluminosilicate zeolite.

4. The iron-loaded aluminosilicate zeolite-derived material according to claim 1, wherein a silicon-to-aluminium ratio of the aluminosilicate zeolite-derived material is from about 5 to about 15.

5. The iron-loaded aluminosilicate zeolite-derived material according to claim 1 having a Fe/Al atomic ratio of from about 0.032 to about 0.75.

6. The iron-loaded aluminosilicate zeolite-derived material according to claim 1 having a mesopore volume determined by nitrogen physisorption of >about 0.10 cm.sup.3/g and optionally a total pore volume of >about 0.30 cm.sup.3/g.

7. The iron-loaded aluminosilicate zeolite-derived material according to claim 1 comprising one or more than one of the transition elements selected from the group consisting of Ce, Cu, Mn, Pd and Pt.

8. A washcoat composition comprising an aqueous slurry of an iron-loaded aluminosilicate zeolite-derived material according to claim 1.

9. A honeycomb monolith substrate comprising an iron-loaded aluminosilicate zeolite-derived material according to claim 1, wherein the honeycomb monolith substrate is coated with a washcoat composition comprising an aqueous slurry of the iron-loaded aluminosilicate zeolite-derived material or the honeycomb monolith substrate comprises an extrusion of the iron-loaded aluminosilicate zeolite-derived material.

10. An exhaust system comprising an injector for injecting a nitrogenous reductant from a source of nitrogenous reductant into a flowing exhaust gas and a source of nitrogenous reductant, which injector is disposed upstream from a honeycomb monolith substrate according to claim 9.

11. The exhaust system according to claim 10 comprising a honeycomb monolith substrate comprising an oxidation catalyst for oxidising nitrogen monoxide in an exhaust gas flowing in the system to nitrogen dioxide, which honeycomb monolith substrate comprising the oxidation catalyst is disposed upstream of the honeycomb monolith substrate comprising the iron-loaded aluminosilicate zeolite-derived material.

Description

(1) In order that the invention may be more fully understood, reference is made to the following Examples by way of illustration only and with reference to the accompanying drawings, wherein:

(2) FIG. 1 is a schematic diagram showing the procedure for a synthetic aluminosilicate CHA embodiment according to the invention performed on SSZ-13;

(3) FIG. 2 shows a comparison of the powder XRD pattern of the parent SSZ-13 and post-synthesis modified materials at various steps of the procedure set out schematically in FIG. 1;

(4) FIG. 3 shows nitrogen physisorption analysis of the parent SSZ-13 and post-synthesis modified SSZ-13 zeolites according to the Examples;

(5) FIG. 4 shows a series of SEM images of (a) H_CHA22, (b) CHA22_DR, (c) CHA22_DR_Fe1, and (d) CHA22_DR_Fe1_SAC materials according to the Examples;

(6) FIG. 5 shows UV-Vis spectra of (a) CHA22_Fe1, (b) CHA22_DR_Fe1, and (c) CHA22_DR_Fe1 SAC; and

(7) FIG. 6 shows the NH.sub.3-selective catalytic reduction (SCR) catalytic performance of CHA22_Fe1, CHA22_DR_Fe1 and CHA22_DR_Fe1 SAC.

(8) Herein we report a method for the synthesis of Fe-SSZ-13 by post-synthesis treatment methods which has been systematically described in the scheme of FIG. 1. First SSZ-13 zeolite is desilicated to generate mesopores and the dissolved silica is reassembled around micelles. Upon pH reduction, the mesoporous silica is deposited on the external surface of mesoporous SSZ-13 zeolite. The resultant mesoporous SSZ-13 zeolite exhibits very high mesoporosity. Thus, the accessibility of the iron species to the inside of SSZ-13 crystals is enhanced and homogeneous distribution of iron ions can be obtained in SSZ-13 crystals. The mesoporous SSZ-13 is then impregnated with iron nitrate and structure directing agent (TMAdOH) solution and then dried. Finely grounded powder was crystallised in the presence of steam.

EXAMPLES

Example 1—Preparation of Fe-CHA Catalyst from Synthetic Aluminosilicate SSZ-13

(9) A commercially available SSZ-13 zeolite (H-form) with a nominal SiO.sub.2/Al.sub.2O.sub.3 ratio (SAR) of 22 was used in the course of these Examples. The as-received sample was labelled as H_CHA22. The Si/Al ratio of the H_CHA22 sample measured by ICP-OES (using inductively couple plasma optical emission spectroscopy) was 11.4, i.e. a silica-to-alumina ratio of 22.8.

Preparation of Mesoporous SSZ-13 Zeolite

(10) A mesoporous SSZ-13 zeolite prepared by a desilication-reassembly method was made as follows. 45 ml of 0.2 M NaOH solution was used to treat 1.0 g of zeolite powder under stirring condition. The treatment was carried out at 65° C. for 1 hour. 0.7 g of Cetyl Trimethyl Ammonium Bromide (CTAB) was dissolved in 45 ml water and added to the above mixture. The pH of the mixture was adjusted to 9 using 1 M HCl and then the mixture was hydrothermally treated at 100° C. for 24 hours under static conditions. The product was then recovered by filtration, washed with distilled water and subsequently dried at 70° C. for 24 hours. Finally, the product was calcined at 550° C. in the presence of air for 8 hours. The mesoporous sample is labelled as CHA22_DR.

Wet Ion Exchange of Microporous and Mesoporous SSZ-13

(11) 1 g of microporous SSZ-13 (H_CHA22) was ion exchanged with 18 ml of 0.01M Fe(NO.sub.3).sub.3.9H.sub.2O at room temperature for 24 hours. The excess water was evaporated and dried in an oven at 60° C. The product was filtered, washed, dried in an oven at 70° C. for 24 hours and calcined at 550° C. in the presence of synthetic air. This sample was labelled as CHA22_Fe1.

(12) The mesoporous SSZ-13 prepared as described hereinabove was first converted into its H-form. Typically, 1 g of sodium form zeolite powder was ion exchanged two times with 25 ml of 0.2 M NH.sub.4NO.sub.3 at room temperature under stirring condition for 24 hours. The ion-exchanged powder was filtered, washed and dried at 70° C. overnight. Subsequently, the post modified sample was calcined in air at 550° C. for 5 hours. Wet ion exchange of sample CHA22_DR (H-form) was performed in a similar manner to that described for the microporous SSZ-13 (CHA22_Fe1). The iron containing mesoporous SSZ-13 prepared by wet ion-exchange was labelled as CHA22_DR_Fe1.

Steam Assisted Crystallisation

(13) Mesoporous SSZ-13 (CHA22_DR) was mixed with an aqueous solution of iron nitrate, water, structure directing agent (TMAdOH) and sodium hydroxide so that the final composition had the composition 1SiO.sub.2:0.05Al.sub.2O.sub.3:0.007Fe.sub.2O.sub.3:0.07Na.sub.2O:0.1TMAdOH:45H.sub.2O. The mixture was stirred for 30 minutes at room temperature. Thereafter, the excess water was evaporated and dried at 60° C. in an oven. The dried powder was finely ground in a mortar using a pestle and the resulting ground powder was poured into a PTFE crucible. Water was added into the liner and the crucible was mounted in the liner. Steam assisted crystallisation was performed at 190° C. for 48 hours. The product was filtered, washed with distilled water and dried in an oven at 70° C. for 24 hours. Finally, the product was calcined in air at 550° C. for 8 hours. To convert the sodium form sample into H-form, 1 g of sodium form zeolite powder was ion-exchanged two times with 25 ml of 0.2 M NH.sub.4NO.sub.3 at room temperature under stirring condition for 24 hours. The ion-exchanged powder was filtered, washed and dried at 70° C. overnight. Subsequently the post-modified sample was calcined in air at 550° C. for 5 hours. The resulting product was labelled as CHA22_DR_Fe1_SAC and had a white colour.

Example 2—Catalyst Characterization

(14) All post-synthesised samples were characterized by XRD (X-Ray diffraction), N.sub.2-physisorption, NH.sub.3-TPD (temperature programmed desorption of ammonia), ICP-OES

(15) (Inductive coupled plasma-optical emission spectroscopy), SEM (Scanning electron microscopy), .sup.29Si and .sup.27Al MAS NMR (Magic-angle spinning nuclear magnetic spectroscopy) and UV-Vis spectroscopy.

(16) XRD of samples was performed using CuK.sub.α radiation on X'Pert Pro diffractometer (Philips Analytical). A diffraction pattern was collected in the 2θ of 2-50° region. The parent sample (H_CHA22) was used as a standard to calculate the relative crystallinity of the post modified samples.

(17) N.sub.2-physisorption at 77 Kelvin was performed in a Quadrasorb™ SI gas adsorption analyser for the surface area analysis and pore size analysis. Prior to analysis, the samples were pre-treated for 12 hours at 300° C. under vacuum.

(18) For NH.sub.3-TPD, the ammonia uptake of all samples was measured using TPDRO 1100 Thermo electron cooperation. Each sample was placed between layers of quartz wool in a glass tube and then pre-treated in the helium flow at 550° C. for 30 minutes with a ramp-rate of 10° C./min. The saturation of each zeolite sample with gaseous ammonia was carried out at 120° C. for 30 minutes. Finally, the ammonia was removed in the helium flow at 600° C. for 60 minutes with a ramp-rate of 10° C./min. The gas exiting the glass tube was analysed using a thermal conductivity detector (TCD).

(19) SEM analysis was performed using a Carl Zeiss ULTRA 55 microscope at a voltage of 3 kV without any sample pre-treatment.

(20) Solid state NMR analyses were performed at 11.74 T on an Agilent DD2 500 MHz WB spectrometer equipped with a commercial 3.2 mm triple resonance MAS probe at a .sup.29Si and .sup.27Al frequency of 99.362 MHz and 130.318 MHz, respectively. .sup.29Si direct excitation experiments of were acquired using a 90° pulse length of 3.0 μs, recycle delay of 60 seconds and at a sample spinning frequency of 10 kHz. Similarly, .sup.27Al magic-angle spinning (MAS) NMR spectra were obtained using direct excitation at a spin speed 15 kHz with a pulse length of 1.25 μs and a recycle delay of 1.0 seconds. .sup.29Si and .sup.27Al MAS experiments were performed with a total number of scans (NS) of 128 and 4000, respectively. .sup.27Al chemical shifts were reported with respect to a solution of AlCl.sub.3 adjusted to a pH of 1 with HCl (delta_iso=0 ppm). Similarly, the Chemical Shifts of .sup.29Si were reported using delta scale and are referenced to tetramethylsilane (TMS) at 0 ppm.

(21) UV-vis spectra were recorded on a Jasco V650 High resolution UV-Vis spectrometer equipped with Harrick Praying Mantis™ Diffuse Reflection accessory and BaSO.sub.4 was used as a reference sample.

Physicochemical Characterisation

(22) FIG. 2 shows the powder XRD pattern of the parent SSZ-13 (H_CHA22), iron containing samples prepared by wet ion-exchange of microporous SSZ-13 (CHA22_Fe1), iron-loaded sample prepared by wet ion exchange of mesoporous SSZ-13 (CHA22_DR_Fe1) and iron-loaded sample prepared by steam-assisted crystallisation of the iron-loaded mesoporous SSZ-13 (CHA22_DR_Fe1 SAC). The corresponding relative crystallinity of the ratio of the integral intensities of X-ray peaks in 2θ°=13.1, 16.3, 18.1, 20.9, 25.4, 26.3, 31.1, and 31.6 are listed in Table 1.

(23) TABLE-US-00002 TABLE 1 Relative crystallinity, chemical composition and acidic properties of the parent and post treated zeolites Relative crystal- Total acidity linity Fe μmol− Samples (%).sup.a Si/Al.sup.b (wt. %) (NH.sub.3/g.sub.cat).sup.c H_CHA 22 100 11.4 0.0 1110 CHA22_DR 11 9.7 0.0 No data CHA_22 Fe1 71 11.1 0.75 1011 CHA22_DR_Fe1 13 11.6 1.1  658 CHA22_DR_Fe1_SAC 59 11.5 0.97 1030 .sup.aRelative crystallinity calculated from the ratio of intensities of X-ray peaks in 2θ° = 13.1, 16.3, 18.1, 20.9, 25.4, 26.3, 31.1, and 31.6 region; .sup.bInductively coupled plasma-optical emission spectroscopy (ICP-OES); and .sup.cCalculated from high temperature peak of the ammonia temperature programmed desorption (NH.sub.3-TPD).

(24) XRD analysis indicates that the parent sample (H_CHA22) has Chabazite (CHA)-type structure without any other crystalline phase. After ion exchange of sample H_CHA22 with iron nitrate solution, the peak intensities characteristic of CHA reflections decreased, possibly due to the higher X-rays absorption coefficient of iron species. The introduction of mesopores and addition of iron in mesoporous SSZ-13 (CHA22_DR_Fe1) leads to interruption in the long range periodic arrangement of crystalline structure and thus results in the reduction of peak intensities.

(25) The sample prepared by steam assisted crystallisation of the iron-loaded mesoporous SSZ-13 exhibits high characteristic peak intensity, which implies that the iron-loaded mesoporous SSZ-13 has been successfully recrystallized.

(26) Nitrogen adsorption-desorption isotherms of the parent sample (H_CHA22), iron-loaded sample prepared by wet ion exchange of microporous SSZ-13 (CHA22_Fe1), mesoporous SSZ-13 (CHA22_DR) and the sample prepared by steam-assisted crystallisation of iron-loaded mesoporous SSZ-13 (CHA22_DR_Fe1 SAC) are presented in FIG. 3 and the corresponding values are listed in Table 2.

(27) TABLE-US-00003 S.sub.BET V.sub.Total V.sub.micro V.sub.meso Samples (m.sup.2/g) (cm.sup.3/g).sup.a (cm.sup.3/g).sup.b (cm.sup.3/g).sup.c H_CHA 22 667 0.36 0.30 0.06 CHA22_DR 576 0.31 0.26 0.05 CHA_22 Fe1 851 0.90 0.05 0.85 CHA22_DR_Fe1 529 0.61 0.03 0.58 CHA22_DR_Fe1_SAC 521 0.40 0.23 0.17 .sup.aV.sub.Total: Total pore volume @ P/P.sub.o = 0.99; .sup.bt-plot; .sup.cV.sub.meso = V.sub.Total − V.sub.micro; and V.sub.meso: Mesopore volume, V.sub.micro: Micropore volume

(28) The nitrogen adsorption isotherm of H_CHA22 follows the IUPAC Type 1 isotherm and implies that the sample has a microporous nature. The pore size distribution of sample H_CHA22 shows that the presence of mesopores is negligible. Addition of iron in sample H_CHA22 results in less BET surface area and micropore volume.

(29) Sample CHA22_DR has high nitrogen uptake in the range of P/Po=0.3-0.45, which indicates the presence of ordered mesopores and can be seen in pore size distribution (FIG. 3 inset). The nitrogen adsorption-desorption isotherm of sample CHA22_DR_Fe1 SAC has high nitrogen uptake at low P/Po and a plateau with increasing P/Po, which indicates that the mesopores which were created by desilication-reassembly are closed after the steam-assisted crystallisation.

(30) The elemental analysis and the acidity measurement of the parent and post-treated samples are given in Table 1. ICP analysis showed that the Si/Al ratio of the mesoporous samples prepared by the desilication-reassembly approach (CHA22_DR) is similar to the parent sample (H_CHA22). The sample prepared by steam-assisted crystallisation of the iron containing mesoporous SSZ-13 zeolite is also similar to the parent sample, which indicates that little or no material is lost during the steam-assisted crystallisation. The iron contents of samples CHA22_Fe1, CHA22_DR_Fe1 and CHA22_DR_Fe1 SAC are 0.75, 1.1 and 0.97 wt. % respectively.

(31) The SEM image analysis shows that the parent sample (H_CHA22) exhibits cube like intergrown morphology of the chabazite (CHA) that appears to have a smooth surface (see FIG. 4a). The amorphous silica can be observed on the external surface of the mesoporous SSZ-13 and iron-loaded mesoporous SSZ-13 zeolites (see FIGS. 4b and 4c respectively). After steam-assisted crystallisation, the amorphous silica fragments are diminished (see FIG. 4d). However there exist some crystals having a rough surface relative to the parent sample (H_CHA22). Nitrogen sorption analysis shows that sample CHA22_DR_Fe1 SAC does not have any intercrystal porosity.

(32) The .sup.29Si MAS NMR values corresponding to the spectra (not shown) of samples H_CHA22, CHA22_DR and CHA22_DR_Fe1 SAC are listed in Table 2 hereinabove. The parent sample (H_CHA22) has two clear peaks at σ=−116 ppm and −110 ppm, which are typically assigned to Q4(0A1) and Q4(1A1). A sharp peak at σ=−116 ppm indicates that 67% silicon atoms are present as Si(SiO).sub.4 groups, and a less intense peak at σ=−110 ppm indicates that 33% silicon atoms are present as AlOSi(SiO).sub.3 groups. A very weak signal at σ=−104 ppm might indicate some defects and is ignored during quantification. Sample CHA22_DR shows three moderate peaks at σ=−116, 110 and 104 ppm which reveal that the Si(SiO).sub.4 groups are decreased from 67 to 42% and structural defects possibly caused by the desilication-reassembly process. These structural defects were annealed by subsequent steam-assisted crystallisation.

(33) .sup.29Al MAS NMR spectra (not shown) of samples H_CHA22, CHA22_DR and CHA22_DR_Fe1 SAC reveal resonance at σ=0 ppm, 30 ppm and 58 ppm, which indicate octahedrally-, pentahedrally-, and tetrahedrally-coordinated aluminium respectively. The parent sample (H_CHA22) shows a sharp peak at 58 ppm, and a small peak at 0 ppm, which indicates that aluminium is predominantly present as framework (81%), gives rise to Si—(OH)—Al bridges and results in high ammonia uptake. The 27Al MAS NMR spectra of mesoporous SSZ-13 zeolite (CHA22_DR) contains an intense peak at 58 ppm (tetrahedrally-coordinated aluminium), which is accompanied by a shoulder that stretches to 30 ppm and indicates the presence of pentahedrally-coordinated aluminium. Octahedrally-coordinated aluminium (σ=0 ppm) is also accompanied by a weak shoulder at 10 ppm, which disappears after steam-assisted crystallisation. Furthermore, sample CHA22_DR_Fe1 SAC has a narrow peak at σ=60 ppm compared to sample CHA22_DR.

(34) UV-vis spectroscopy was used to investigate the coordination state and extent of aggregation of iron species. The UV-vis spectra of samples CHA22_Fe1, CHA22_DR_Fe1, and CHA22_DR_Fe1 SAC are shown in FIG. 5. The UV-vis spectrum of sample CHA22_Fe1 (which was prepared by wet ion exchange of microporous SSZ-13 zeolite) is stretched from 200 to 600 nm, which indicates various d-d transitions and thus that the sample contains the various types of iron sites. Three narrow and strong bands can be observed at low wavelength: narrow band which is centered at 220 nm indicates isolated tetrahedrally-coordinated Fe.sup.3+ sites; a narrow band centered at 280 nm indicates isolated octahedrally-coordinated Fe.sup.3+ sites; and a narrow band at 340 nm can be assigned to oligomeric Fe.sup.3+ sites. This sample was prepared by simple wet ion exchange of microporous SSZ-13 zeolite and additionally shows two broad bands at 427 and 540 nm, which can be assigned to larger iron oxide particles (Fe.sub.2O.sub.3-like aggregates).

(35) The Sample CHA22_DR_Fe1 has clear bands at 280 and 340 nm, which are indicators of isolated octahedrally-coordinated and oligomeric Fe.sup.3+ sites, respectively. However, the low wavelength band from 200-220 nm is not clear, probably because this sample was prepared by wet ion exchange of mesoporous SSZ-13 (CHA22_DR), which has very low microporosity (0.05 cm.sup.3/g). The two bands at 427 and 540 nm, for the larger iron oxide particles, are much weaker than the corresponding bands in sample CHA22_Fe1, which suggests that the iron ions supported in mesoporous SSZ-13 (CHA22_DR_Fe1) were less oxidised during calcination. Without wishing to be bound by theory, the inventors speculate that a reason for this observation may be because, in the CHA22_Fe1 sample, a significant fraction of iron ions could not diffuse into the micropores of SSZ-13, and thus were more likely to be oxidised during calcination.

(36) The UV-vis band of sample CHA22_DR_Fe1 SAC extends from 200 to 500 nm and shows strong, defined peaks at 220 and 280 nm, which indicate isolated tetrahedrally-/and octahedrally-coordinated Fe.sup.3+ sites and are difficult to discriminate therebetween. Moreover, this sample has a weak band at 340 nm and so a relatively small quantity of oligomeric Fe.sup.3+ sites. A very weak signal at 470 nm implies that sample CHA22_DR_Fe1 SAC contains negligible iron oxide particles.

Example 3—Catalytic Activity Measurement

(37) The NH.sub.3-SCR catalytic activity of each sample was measured in a fixed bed quartz reactor. The composition of the reactant gas mixture used was 550 ppm NH.sub.3, 500 ppm NO, 8% O.sub.2, 10% H.sub.2O with a balance of nitrogen. The total gas flow rate was 840 ml/h or 1000 L/g.Math.h WHSV (weight hourly space velocity) and a sample mass of 50 mg was used. Prior to collecting reaction measurements, all samples were pre-treated at 550° C. in air for 30 min. The gas composition was measured using a Varain FT-IR equipped with gas cell (Gemini MARS) having a 4 m path length. The catalytic activity was measured from 325° C. to 500° C. with an interval of 25° C. and a waiting (or “soak”) time of 45 minutes at each temperature.

(38) The catalytic activity of the CHA22_Fe1, CHA22_DR_Fe1 and CHA22_DR_Fe1 SAC samples were tested and the results are presented in FIG. 6. Samples CHA22_Fe1 and CHA22_DR_Fe1, have very low NO and NH.sub.3 conversion. These samples were prepared by wet ion exchange of microporous SSZ-13 and mesoporous SSZ-13 respectively with iron nitrate solution. It can be seen from the results shown in Table 1 that sample CHA22_Fe1 has relatively high crystallinity and micropore volume, and the UV-vis data (not shown) indicates that some iron is present as isolated tetrahedrally-coordinated or octahedrally-coordinated sites and oligomeric Fe.sup.3+ sites together with a significant amount of iron oxide aggregate particles. These iron oxide aggregates do not appear to be active for the NH.sub.3-SCR reaction and so this sample has a relatively low NO conversion.

(39) Iron-loaded mesoporous SSZ-13 (CHA22_DR_Fe1) also exhibits relatively low NO conversion, although it contains a relatively high wt. % quantity of iron. This relatively low NO conversion is presumably due to the loss of crystalline structure during the desilication-reassembly process and thus can be observed in the XRD and nitrogen physisorption results (see FIGS. 2 and 3 and under the “Physicochemical Characterisation” heading of Example 2).

(40) Sample CHA22_DR_Fe1 SAC exhibits good, relatively high NO conversion compared to the other two samples which we attribute to the presence of iron sites in SSZ-13 cages as isolated tetrahedrally-coordinated and octahedrally-coordinated and comparatively fewer oligomeric Fe.sup.3+ sites.

(41) The foregoing detailed description has been provided by way of explanation and illustration and is not intended to limit the scope of the appended claims. Many variations in the presently preferred embodiments illustrated herein will be apparent to one of ordinary skill in the art and remain within the scope of the appended claims and their equivalents.

(42) For the avoidance of doubt, the entire contents of all documents acknowledged herein are incorporated herein by reference.