Comparative study of zeolite catalyzed alkylation of ben-zenewith alcohols of different chain length: H-ZSM-5 versusmordenite, Catal. Today204 (2013) 73–84.[24] J.R. Anderson, T. Mole, V. Christov, A novel effect of shape selectivity: moleculartraffic control in zeolite ZSM-5, J. Catal. 61 (1980) 477–484.[25] C.H. Christensen, K. Johannsen, E. Toernqvist, I. Schmidt, H. Topsoe, Mesoporous ze-olite single crystal catalysts: diffusion and catalysis in hierarchical zeolites, Catal.Today 128 (2007) 117–122.[26] C.H. Christensen, K. Johannsen, I. Schmidt, Catalytic benzene alkylation over meso-porous zeolite single crystals: improving activity and selectivity with a new familyof porous materials, J. Am. Chem. Soc. 125 (2003) 13370–13371.[27] K. Egeblad, C.H. Christensen, M. Kustova, Templating mesoporous zeolites, Chem.Mater. 20 (2008) 946–960.[28] K. Na, M. Choi, R. Ryoo, Recent advances in the synthesis of hierarchicallynanoporous zeolites, Microporous Mesoporous Mater. 166 (2013) 3–19.[29] J. Perez-Ramirez, C.H. Christensen, K. Egeblad, J.C. Groen, Hierarchical zeolites:enhanced utilisation of microporous crystals in catalysis by advances in materialsdesign, Chem.Soc.Rev. 37 (2008) 2530–2542.[30] K. Na, C. Jo, J. Kim, K. Cho, J. Jung, Y. Seo, R.J. Messinger, B.F. Chmelka, R. Ryoo,Directing zeolite structures into hierarchically nanoporous architectures, Science333 (2011) 328–332.[31] M. Choi, K. Na, J. Kim, Y. Sakamoto, O. Terasaki, R. Ryoo, Stable single-unit-cell nano-sheets of zeolite MFI as active and long-lived catalysts, Nature 461 (2009) 246–249.[32] K. Moller, B. Yilmaz, R.M. Jacubinas, U. Muller, T. Bein, One-step synthesis of hierar-chical zeolite Beta via network formation of uniform nanocrystals, J. Am. Chem. Soc.133 (2011) 5284–5295.[33] F.S. Xiao, L.F.Wang, C.Y. Yin, K.F. Lin, Y. Di, J.X. Li, R.R. Xu, D.S. Su, R. Schlogl, T. Yokoi,T. Tatsumi, Catalytic properties of hierarchical mesoporous zeolites templated witha mixture of small organic ammonium salts and mesoscale cationic polymers,Angew. Chem. Int. Ed. 45 (2006) 3090–3093.[34] D.H. Park, S.S. Kim, T.J. Pinnavaia, F. Tzompantzi, J. Prince, J.S. Valente, Selectiveisobutene oligomerization by mesoporous MSU-SBEA catalysts, J. Phys. Chem. C115 (2011) 5809–5816.[35] M.S. Holm, E. Taarning, K. Egeblad, C.H. Christensen, Catalysis with hierarchical zeo-lites, Catal. Today 168 (2011) 3–16.[36] S.L. Jahn, D. Cardoso, Influence of the Si/Al ratio and ZSM-5 crystallite size on themethylation of toluene, Catal. Today 5(1989)515–521.[37] C. Ding, X. Wang, X. Guo, S. Zhang, Characterization and catalytic alkylation of hy-drothermally dealuminated nanoscale ZSM-5 zeolite catalyst, Catal. Commun. 9(2008) 487–493.[38] L.B. Young, S.A. Butter,W.W. Kaeding, Shape selective reactions with zeolite catalysts:III. Selectivity in xylene isomerization, toluene-methanol alkylation, and toluene dis-proportionation over ZSM-5 zeolite catalysts, J. Catal. 76 (1982) 418–432.[39] O.C. Gobin, S.J. Reitmeier, A. Jentys, J.A. Lercher,Comparisonofthetransportofaromaticcompounds in small and large MFI particles, J. Phys. Chem. C 113 (2009) 20435–20444.[40] O.C. Gobin, S.J. Reitmeier, A. Jentys,J.A.Lercher,Diffusionpathwaysofbenzene, toluene and p-xylene in MFI, Microporous Mesoporous Mater. 125(2009) 3–10.[41] S.J. Reitmeier, R.R. Mukti, A. Jentys, J.A. Lercher, Surface transport processes andsticking probability of aromatic molecules in HZSM-5, J. Phys. Chem. C 112 (2008)2538–2544.[42] E.G. Derouane, Z. Gabelica, A novel effect of shape selectivity: molecular trafficcon-trol in zeolite ZSM-5, J. Catal. 65 (1980) 486–489.[43] L. Karwacki, M.H.F. Kox, D.A. Matthijs de Winter, M.R. Drury, J.D. Meeldijk, E.Stavitski, W. Schmidt, M. Mertens, P. Cubillas, N. John, A. Chan, N. Kahn, S.R. Bare,M. Anderson, J. Kornatowski, B.M. Weckhuysen, Morphology-dependent zeoliteintergrowth structures leading to distinct internal and outer-surface molecular dif-fusion barriers, Nat. Mater. 8(2009)959–965.[44] K. Zhu, J. Sun, J. Liu, L. Wang, H. Wan, J. Hu, Y. Wang, C.H.F. Peden, Z. Nie, Solventevaporation assisted preparation of oriented nanocrystalline mesoporous MFI zeo-lites, ACS Catal. 1(2011)682–690.[45] P.L. Llewellyn, J.P. Coulomb, Y. Grillet, J. Patarin, G. Andre, J. Rouquerol, AdsorptionbyMFI-type zeolites examined by isothermalmicrocalorimetry and neutron diffrac-tion. 2. Nitrogen and carbon monoxide, Langmuir 9 (1993) 1852–1856.[46] J.C. Groen, L.A.A. Peffer, J. Perez-Ramirez, Pore size determination inmodifiedmicro-and mesoporous materials. Pitfalls and limitations in gas adsorption data analysis,Microporous Mesoporous Mater. 60 (2003) 1–17.[47] J.C. Jansen, F.J. van der Gaag, H. van Bekkum, Identification of ZSM-type and other5-ring containing zeolites by I.R. spectroscopy, Zeolites 4(1984)369–372.[48] B. Liu, C. Li, Y. Ren, Y. Tan, H. Xi, Y. Qian, Direct synthesis of mesoporous ZSM-5zeolite by a dual-functional surfactant approach, Chem. Eng. J. 210 (2012) 96–102.[49] B.T. Holland, Transformation of mostly amorphous mesoscopic aluminosilicate col-loids into high surface area mesoporous ZSM-5, Microporous Mesoporous Mater. 89(2006) 291–299.[50] K. Barbera, F. Bonino, S. Bordiga, T.V.W. Janssens, P. Beato, Structure–deactivation re-lationship for ZSM-5 catalysts governed by framework defects, J. Catal. 280 (2011)196–205.[51] F. Lónyi, J. Valyon, On the interpretation of the NH3-TPD patterns of H-ZSM-5 andH-mordenite, Microporous Mesoporous Mater. 47 (2001) 293–301.[52] G. Bagnasco, Improving the selectivity of NH3-TPD measurements, J. Catal. 159(1996) 249–252.[53] E.W. Thiele, Relation between catalytic activity and size of particle, Ind. Eng. Chem.31 (1939) 916–920.
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