APPLICATION OF INTERFERENCE AND IR MICROSCOPY FOR STUDIES OF INTRACRYSTALLINE MOLECULAR TRANSPORT IN AFI TYPE ZEOLITES C. CHMELIK, E. LEHMANN, S. VASENKOV, B. STAUDTE, J. KÄRGER Universität Leipzig, Institut für Physik, Linnéstr. 5, D-04103, Leipzig, Germany Abstract Interference microscopy (IFM) and FTIR microscopy (IRM) are applied to study intracrystalline concentration profiles in SAPO-5 and CrAPO-5 zeolite crystals. By using both techniques, the high spatial resolution of interference microscopy is complemented by the ability of FTIR spectroscopy to pinpoint adsorbates by their characteristic IR bands. Intracrystalline concentration profiles of water, adsorbed in large crystals of CrAPO-5 and SAPO-5 under equilibrium with water vapor at 1 and 20 mbar, were determined with use of interference microscopy. At lower pressure, the profiles reveal highly inhomogeneous distributions of intracrystalline water in both types of crystal. This effect is attributed to structural heterogeneity of the crystals. The structural heterogeneity has been found to have a low or no influence on the final uptake level at 20 mbar of the crystals. Concentration profiles of methanol during its adsorption into the onedimensional channels of CrAPO-5 crystals are reported. The exceptionally high spatial resolution allowed us to obtain detailed information on the interplay of intracrystalline diffusion, the permeability of the crystal surface and the role of the internal structure on molecule uptake. 1. Introduction Due to their regular structure and a well-defined morphology zeolites are broadly used as catalysts and molecular sieves in different fields of applied chemistry and technology. Considering diffusion, due to simplicity of the framework topology, a zeolite consisting of a packing of oriented cylinders (viz. AFI type) represents an ideal model system for investigations of the intracrystalline transport [1]. 1 While the ideal structure of zeolites is routinely used to elucidate their adsorption and transport properties it was only recently appreciated that these properties can be influenced to a great extent by building defects of the crystals [2,3]. Investigation of intergrowth effects in zeolites is particularly important since these phenomena may strongly influence molecular uptake and intracrystalline diffusion. Such investigations are also important in view of the persistent differences between intra-crystalline diffusivities obtained for the same zeolites by various experimental techniques [2,3]. In the present work interference microscopy (IFM) and IR microscopy (IRM) are applied to study the internal structure of zeolite crystals as well as the influence of this structure on intracrystalline molecular transport. 2. Experimental section The measurements were carried out by applying the only two techniques, which have been proved to be suitable for studies of intracrystalline concentration profiles of guests in zeolite crystals [4-8]. The first one is the interference microscopy technique (IFM), which has been recently introduced in our laboratory. It is based on following the change of the refractive index of a zeolite crystal during molecular adsorption or desorption. Due to the proportionality of the refractive index and the local concentration of guest molecules in the crystal it is possible to monitor the concentration integrals in the direction of observation. The concentration integrals were also monitored in a somewhat more direct way by using the IR microscopy method (IRM). Despite a poor spatial resolution, IR microscopy presents an extremely useful tool to study intracrystalline concentration profiles due to its ability to distinguish between different adsorbates. Thus, it opens the possibility for tracer-exchange measurements. For the measurements and activation the zeolite sample was introduced into a specially made optical or IR cell, which was connected to the vacuum system. The adsorption, desorption or tracer exchange was achieved by appropriate changes of adsorbate pressure in the surrounding gas phase. 3. Results and discussion 3.1. METHANOL IN CrAPO-5: EQUILIBRIUM WITH THE VAPOR PHASE The IFM equilibrium concentration profiles at a pressure of 1 mbar are shown in Figure 1a. These non-homogenous profiles can not be explained by using the ideal textbook structure [1]. In view of the image obtained for an unloaded 2 crystal under crossed Nicols we ascribe these non-homogeneous profiles to the influence of regular intergrowth effects. They render parts of the channel system to be inaccessible for methanol molecules. Based upon the concentration profiles we propose an internal structure schematically shown in Figure 1c [7]. To confirm the IFM results concentration profiles of methanol in CrAPO5 crystals were recorded under the same measurement conditions by IRM. Onedimensional concentration profiles were compared. Figure 1b demonstrates the good agreement between the results obtained by both techniques [7]. Figure 1. (a) IFM equilibrium intracrystalline concentration profile of methanol in a CrAPO-5 crystal. The color intensity is proportional to the integrals of local concentration. (b) Comparison of mean concentration integrals I recorded by IRM and IFM. (c) Suggested internal structure. The channel direction coincides with the z direction. 3.2. METHANOL IN CrAPO-5: UPTAKE KINETICS The primary aim of the dynamic Monte Carlo simulations was to investigate quantitatively the influence of the intergrowth structure and the transport barriers on the crystal surface on the intracrystalline transport (figure 2). The used simulations are analogous to the numerical solution of Fick’s second-law- 3 type equations for diffusion in one-dimensional channels (accessible part only) with transport barriers at the channel edges. Comparing the simulations and experimental results we finally obtain the value of D=0.43x10-12 m2/s for the intracrystalline diffusivity of methanol in the limit of small loadings and can estimate the rate constant of barrier penetration to α=0.35x10-7 m/s. (a) (b) Assumptions (MC): 1.one-dimensional random walk in the lattice 2. probability of diffusion step is independent of concentration Figure 2. (b) Intracrystalline concentration of methanol, integrated along the y crystallographic direction in CrAPO-5 at different times after the start of the methanol adsorption. The profiles were obtained by IFM (black line) and by the dynamic MC method (broken line). (a) The internal structure of CrAPO-5 crystals (shown only for the lower part of the crystal). x, y and z are the crystallographic directions. The broken lines outline the observation plane of the IFM measurements of the transient profiles with the arrow indicating the direction of observation. 4 The reported results show that the estimated value of the diffusion coefficient D is around a factor of 2 smaller than that of L*α (L - crystal size in z-direction). This indicates that the rate of methanol uptake is mainly determined by the intracrystalline diffusivity of methanol. However, this rate is somewhat reduced due to existence of transport barriers on the crystal surface [9]. 3.3. WATER IN CrAPO-5 AND SAPO-5: EQUILIBRIUM WITH THE VAPOR PHASE Figure 3 shows the intracrystalline concentration profiles of water in the CrAPO-5 and SAPO-5 measured by IFM. It is seen that the profiles obtained for low pressure of 1 mbar reveal highly inhomogeneous, but reproducible patterns [10]. Noteworthy is that the profile in CrAPO-5 (figure 3 a1, a3) resembles, to some extent, the methanol profile observed for these crystals (figure 1a). Apparently, the explanation might also be applied to water. The origin of the intergrowth effects may be derived from the progress of the crystal growth process. As has been shown in ref. [11] the dumbbell shape is characteristic of some AFI-type crystals in the intermediate stage of growth. Figure 3. Intracrystalline concentration profiles of water in the CrAPO-5 (a1, a2, a3) and SAPO-5 (b1, b2, b3) crystals integrated along the y direction under equilibrium with water vapor at 1 mbar (a1, b1, a3, b3) and 20 mbar (a2, b2). The channels run along the z axis. Darker regions correspond to higher concentration integrals. 5 The increase in water vapor pressure to 20 mbar results in an essentially homogeneous profile in CrAPO-5 (figure 4 a2), i.g. all the crystal constituents are equally filled with liquid-like water.. Imaginable structural factors which can influence the intracrystalline water concentration at low water vapor pressure are the content and the distribution of the Cr atoms and/or the presence of defect sites. The inhomogeneous profiles of water in SAPO-5 may result from a structural heterogeneity of the crystals as well. For SAPO-5 has been indicated by electron microprobe analysis that the silicon content of the central part of the crystals was lower by a factor of 2 to 3 than that at the crystal margin [12]. By studying the progress of crystal growth it was found that “pencil-like” crystals are formed initially, later the tips of the “pencils” flatten out proceeding with a much higher consumption of silicon than the initial one. At the high water vapor pressure the condensation of water and the volume filling of the pores of SAPO-5 occur, which are primarily determined by the accessible pore volume as justified by the homogeneous concentration profile observed at 20 mbar (figure 4 b2). It may be speculated that the crystal components which form at the earlier stages of the growth process, i.e. dumbbell core (CrAPO-5) or “pencil-like” (SAPO-5) core, can adsorb more water than the other crystal parts under the low vapor pressure of water [10]. 4. Conclusion The obtained results show large potentials of the new IRM and IFM methods for elucidation of structural and transport properties of zeolite crystals, particularly when these techniques are combined with dynamic MC simulations. From the experimental evidence provided by these techniques, the real structure of crystals, which reveal perfect shape characteristic for single crystals, has been found to deviate decisively from the textbook structure of the given type of zeolite. Combination of the experimental methods with dynamic MC simulations allowed us to investigate separately the influences of (i) the intracrystalline diffusion, (ii) the transport barriers on the external crystal surface and (iii) the effects of the intergrowth structure on molecular uptake. Acknowledgement We acknowledge Prof. F. Schüth and Dr. Ö. Weiss as well as Dr. J. Kornatowski and Dr. G. Zadrozna for synthesizing and providing us the large zeolite crystals. Financial support by Deutsche Forschungsgemeinschaft (SFB 294 and Graduierten-kolleg “Physikalische Chemie der Grenzflächen”), Fonds der Chemischen Industrie and Max-Buchner-Forschungsstiftung is gratefully acknowledged. 6 References 1. Baerlocher Ch., Meier W.M., Olson D.H. (2001) Atlas of Zeolite Framework Types, Elsevier, Amsterdam, pp. 34-35. 2. Kärger J., Ruthven D.M. (2002) Handbook of Porous Solids, Schüth F., Sing K.S.W., Weitkamp J. (Eds.), Diffusion and Adsorption in Porous Solids, Wiley-VCH, Weinheim, p. 2089. 3. Kärger J., Vasenkov S., Auerbach S. (2003) Handbook of Zeolite Catalysts and Microporous Materials, Auerbach S.M., Carrado K.A.,. Dutta P.K (Eds.), Diffusion in Zeolites, Marcel Dekker, New York, 4. Schemmert U., Kärger J., Krause C., Rakoczy R.A., Weitkamp, J. (1999) Europhys. Lett., 46 204. 5. Schemmert U., Kärger J., Weitkamp J. (1999) Microporous and Mesoporous Materials, 32 101. 6. Geier O., Vasenkov S., Lehmann E., Kärger J., Schemmert U., Rakoczy R.A., Weitkamp J. (2001) J. Phys. Chem. B, 105 10217-10222. 7. Lehmann E., Chmelik C., Scheidt H., Vasenkov S., Staudte B., Kärger J., Kremer F., Zadrozna G., Kornatowski J. (2002) J. Am. Chem. Soc. 124 8690-8692. 8. Geier O., Vasenkov S., Lehmann E., Kärger J., Schemmert U., Rakoczy R.A., Weitkamp J. (2001) Stud. Surf. Sci. Catal., 135 154-160. 9. Lehmann E., Vasenkov S., Kärger J., Zadrozna G., Kornatowski J. (2003) J. Chem. Phys., 118, 6129-6132. 10. Lehmann E., Vasenkov S., Kärger J., Zadrozna G., Kornatowski J., Weiss Ö., Schüth F. (2003) J. Phys. Chem. B, 107, 4685-4687. 11. Klap G.J., Wübbenhorst M., Jansen J.C., van Konigsveld H., van Bekkum H., van Turnhout J. (1999) Chem. Mater. 11, 3497-3503. 12. Schunk S.A., Demuth D.G., Schulz-Dobrick B., Unger K.K., Schüth F. (1996) Microporous Mater., 6, 273-285. 7