COMMUNICATIONS
synthesis or by postchemical treatment.[2] Considering the
channel size, zeolites are classified as ultralarge (>12
membered rings (MR)), large (12-MR), medium (10-MR)
or small (8-MR) pore materials depending on the number of
T atoms that limits the pore aperture of their largest channels
(T represents atoms from the aluminum and silicon families).
While zeolites with small pores have found some specific
applications in, for instance, the conversion of methanol to
olefins[3], the most successful zeolitic catalysts are those based
on zeolites withmedium and large pores. More specifically,
large-pore zeolites have unique properties for dealing with
many of the oil fractions involved in refinery processes
(cracking, hydrocracking, hydroisomerization, among others),
in petrochemistry (including benzene alkylation with olefins,
isomerization and disproportionation of alkylaromatic spe-
cies), and in fine chemical production (such as alkylation,
acylation, isomerization, and esterification).
It must be noted, for many of the processes named above, a
rapid diffusion of the reactants and products is desired and
this is better achieved with large-pore tridirectional zeolites.
Until recently, however, only two large-pore tridirectional
zeolites were synthesized, faujasite and Beta, and of these
only the Beta zeolite can be directly synthesized with a high
Si:Al ratio and therefore does not need, unlike the faujasites,
a postsynthesis dealumination. Therefore, owing to the large
catalytic interest and very limited number of large-pore
tridirectional zeolites, a considerable effort has been devoted
in the last decade to produce such structures[4]. Very
recently,[5] the pure silica form of a new large-pore tridirec-
tional zeolite has been presented, named ITQ-7 (Instituto de
Tecnología Química-7). Unfortunately, the authors were
unable to introduce acidity into ITQ-7 by direct synthesis
with the trivalent (Al and Ga family) atoms in an isomorph-
ically substituted zeolite[6]. Therefore, this large-pore tridirec-
tional zeolite have had no possibilities in catalysis since only
the purely siliceous form was available. Herein, we present
the possibility to synthesize ITQ-7 with different TIII and TIV
elements isomorphically incorporated into the framework
and, in this way, acidic, catalytically active ITQ-7 materials
have been prepared.
[6] M. Sono, M. P. Roach, E. D. Coulter, J. H. Dawson, Chem. Rev. 1996,
96, 2841 ± 2887.
[7] B. J. Wallar, J. D. Lipscomb, Chem. Rev. 1996, 96, 2625 ± 2657.
[8] D. T. Sawyer, A. Sobkowiak, T. Matsushita, Acc. Chem. Res. 1996, 29,
409 ± 416.
[9] M. Newcomb, P. A. Simakov, S.-U. Park, Tetrahedron Lett. 1996, 37,
819 ± 822.
[10] P. A. MacFaul, K. U. Ingold, D. D. M. Wayner, L. Que Jr., J. Am.
Chem. Soc. 1997, 119, 10594 ± 10598.
[11] a) F. Minisci, F. Fontana, S. Araneo, F. Recupero, L. Zhao, Synlett
1996, 119 ± 125; b) D. H. R. Barton, Synlett 1997, 229 ± 230.
[12] B. Meunier, Chem. Rev. 1992, 92, 1411 ± 1456.
[13] M. J. Perkins, Chem. Soc. Rev. 1996, 229 ± 236.
[14] M. Newcomb, P. A. Simakov, S.-U. Park, Tetrahedron Lett. 1996, 37,
819 ± 822.
[15] V. I. Ponomarev, O. S. Filipenko, L. O. Atovmyan, S. A. Bobkova,
Á
K. I. Turte, Sov. Phys. Dokl. 1982, 27, 6 ± 9.
[16] Crystal data for 3 (213 K) withMo
radiation (l 0.71073 ):
Ka
orthorhombic, space group Pccn, a 16.698(5), b 9.074(2), c
16.587(4) , V 2513(1) 3, Z 4, R1 0.0478 for 2156 data with
I > 2s(I), GOF (on F 2) 1.108. For 4 (213 K): orthorhombic, space
group P212121, a 13.3830(1), b 16.4843(2), c 24.1315(2) , V
5323.60(8) 3, Z 4, R1 0.0327 for 9486 data with I > 2s(I), GOF
(on F 2) 1.055. Further details on the crystal structure investigations
may be obtained from the Fachinformationszentrum Karlsruhe, 76344
Eggenstein-Leopoldshafen, Germany (fax: (49)7247-808-666;
e-mail: crysdata@fiz-karlsruhe.de), on quoting the depository num-
bers CSD-411108 (3) and -411109 (4).
[17] F. Minisci, E. Vismara, F. Fontana, Heterocycles 1989, 28, 489 ± 519.
[18] F. Recupero, A. Bravo, H.-R. Bjùrsvik, F. Fontana, F. Minisci, M.
Piredda, J. Chem. Soc. Perkin Trans. 2 1997, 2399 ± 2405.
[19] D. H. R. Barton, F. Halley, N. Ozbalik, M. Schmitt, E. Young, G.
Balavoine, J. Am. Chem. Soc. 1989, 111, 7144 ± 7149.
[20] G. V. Buxton, C. L. Greenstock, W. P. Helman, A. B. Ross, J. Phys.
Chem. Ref. Data 1988, 17, 513 ± 886.
[21] F. Minisci, A. Citterio, E. Vismara, Tetrahedron 1985, 41, 4157 ± 4170.
[22] S. Kiani, A. Tapper, R. J. Staples, P. Stavropoulos, J. Am. Chem. Soc.,
submitted.
[23] D. H. R. Barton, B. Hu, D. K. Taylor, R. U. Rojas Wahl, J. Chem. Soc.
Perkin Trans. 2 1996, 1031 ± 1041.
Synthesis, Characterization, and Catalytic
Activity of a Large-Pore Tridirectional Zeolite,
H-ITQ-7**
The synthesis of isomorphically substituted zeolites was
attempted following two strategies. The first strategy consists
of synthesizing a boron-containing ITQ-7 (B-ITQ-7) sample
which already should present some weak acidity and then, in a
further step, to exchange B with Al to yield materials, named
B/Al-ITQ-7, with a much greater acidity than the B-ITQ-7
precursor. The second strategy involves the direct synthesis of
Al-ITQ-7. The two synthesis routes will be described below.
B-ITQ-7: Boron-containing ITQ-7 was formed from a gel
withthe composition SiO 2:B2O3:C14H26NOH:HF:H2O in a
molar ratio 1.0:0.01:0.50:0.50:3.0, where C14H26NOH is 1,3,3-
trimethyl-6-azonium-tricyclo[3.2.1.46,6]dodecane hydroxide.
The gel was prepared by dissolving H3BO3 (0.08 g) in a
solution of C14H26NOH (0.99m, 31.98 g). Tetraethylorthosili-
cate (TEOS, 13.46 g) was then hydrolyzed in the solution and
the mixture was stirred gently to completely evaporated the
ethanol formed. Finally, HF (1.34 g as 48.1% in water) and
purely siliceous ITQ-7 crystals (0.20 g) were added and the
mixture was homogeneized. After 7 days crystallization at
Â
Ä
Avelino Corma,* María Jose Díaz-Cabanas, and
Vicente Fornes
Â
Zeolites are probably the most widely used solid catalysts in
refining, petrochemistry, and fine chemical production. This is
especially true for the acid zeolites, (H-zeolites). Their success
is derived from properties such as high surface area, high
adsorption capacity, molecular sieve characteristics, and the
possibility of preparation witha well defined number of
uniformly active sites;[1] these sites are introduced by direct
Â
Ä
[*] Prof. A. Corma, M. J. Díaz-Cabanas, V. Fornes
Instituto de Tecnología Química
Â
UPV-CVSIC Universidad Politecnica de Valencia
Avda. de los Naranjos s/n, 46022 Valencia (Spain)
Fax : (34)96-387-78-09
[**] We thank the Spanish CICYT for financial support (Project MAT97-
1016-C02-01).
2346
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Angew. Chem. Int. Ed. 2000, 39, No. 13