Abstract
Maleic anhydride, a precursor to polyester resins, is made by oxidation of n -butane over vanadium phosphate catalysts. This system is of general interest because it is the only heterogeneously catalyzed, alkane-selective oxidation reaction in commercial use. Time-resolved in situ x-ray absorption spectroscopy shows that when either α I -VOPO 4 /SiO 2 or (VO) 2 P 2 O 7 /SiO 2 catalysts are exposed to n -butane, the rate of maleic anhydride formation is proportional to the rate of decay of V 5+ species in the catalyst. Thus V 5+ species are kinetically significant for the production of maleic anhydride and not just for the production of by-products. The results also suggest that V 5+ species may play a role in the initial hydrogen abstraction from n -butane, the rate-determining step in the reaction sequence. V 4+ sites appear to be responsible for by-product formation.
References
24
Referenced
208
- Felthouse T. R., Burnett J. C., Mitchell S. F., Mummy M. J., Kirk-Othmer Encyclopedia of Chemical Technology (Wiley, New York, 1995), pp. 893-928. / Kirk-Othmer Encyclopedia of Chemical Technology by Felthouse T. R. (1995)
-
Mars P., Krevelen D. W. v., Chem. Eng. Sci. 3, 41 (1954).
(
10.1016/S0009-2509(54)80005-4
) / Chem. Eng. Sci. by Mars P. (1954) -
Bej S. K., Rao M. S., Ind. Eng. Chem. Res. 31, 2075 (1992).
(
10.1021/ie00009a002
) / Ind. Eng. Chem. Res. by Bej S. K. (1992) -
Trifiro F., Catal. Today 16, 91 (1993).
(
10.1016/0920-5861(93)85009-O
) / Catal. Today by Trifiro F. (1993) - Misono M., et al., in New Developments in Selective Oxidation, Centi G., Trifiro F., Eds. (Elsevier, Amsterdam, 1990), p. 605. / New Developments in Selective Oxidation by Misono M. (1990)
-
Schiott B., Jorgensen K. A., Catal. Today 16, 79 (1993).
(
10.1016/0920-5861(93)85008-N
) / Catal. Today by Schiott B. (1993) - Centi G., ibid.5. / ibid. by Centi G.
-
Hutchings G. J., Desmartin-Chomel A., Olier R., Volta J. C., Nature 368, 41 (1994).
(
10.1038/368041a0
) / Nature by Hutchings G. J. (1994) - Soejarto A., Schrader G., Coulston G. S., Can. J. Chem. Eng.in press. / Can. J. Chem. Eng. by Soejarto A.
-
Bordes E., Catal. Today 16, 27 (1993).
(
10.1016/0920-5861(93)85003-I
) / Catal. Today by Bordes E. (1993) - Hodnett B. K., ibid.131. / ibid. by Hodnett B. K.
- Ebner J. T., Thompson M. R., ibid.51. / ibid. by Ebner J. T.
-
Gai P. L., Kourtakis K., Science 267, 661 (1995).
(
10.1126/science.267.5198.661
) / Science by Gai P. L. (1995) -
Tamaru K., in Catalysis: Science and Technology, , Anderson J. R., Boudart M., Eds. (Springer-Verlag, Berlin, 1991), pp. 87-129.
(
10.1007/978-3-642-75956-7_2
) / Catalysis: Science and Technology by Tamaru K. (1991) - The α I -VOPO 4 /SiO 2 catalyst was prepared by wet impregnation. Davisil silica (grade 644) was washed in 1 M nitric acid at 80°C for 48 hours and then rinsed repeatedly with doubly deionized water until the washings tested pH neutral. Air calcination at 90°C overnight and subsequently at 520°C for 6 hours removed labile hydroxyls and surface nitrates. The resulting silica had a surface area of 338 m 2 /g determined by the Brunauer-Emmett-Teller (BET) N 2 adsorption method. The silica was impregnated under conditions of incipient wetness with an aqueous solution containing ammonium metavanadate oxalic acid and dibasic ammonium phosphate. The solution concentrations were adjusted to obtain an elemental P:V ratio of 1→1 and a 6 weight % vanadium loading on the silica support. The P:V ratios and loading were confirmed with inductively coupled plasma-optical emission spectroscopy (ICP) and the crystalline phase was confirmed by x-ray diffraction and laser Raman spectroscopy (514 nm). The impregnated silica was dried in air at 90°C overnight at 200°C for 2 hours and finally at 500°C for 6 hours. The resulting material had a 181-m 2 /g surface area. The (VO) 2 P 2 O 7 /SiO 2 catalyst was prepared as follows: 10.42 g of the cluster [(VO) 4 (P 2 O 7 ) 2 (CH 3 O) 4 ] (C 14 H 19 N 2 ) 4 · (CH 3 OH) 4 (16) was dissolved into 50 ml of dry methanol in a glove box. The deep blue solution was impregnated into 10 g silica powder (BET surface area of 300 m 2 /g) and the slurry was evaporated to dryness. The deep blue solid was calcined in flowing air to 350°C for 1 hour and recovered for use in TRXAS experiments. The x-ray absorption and reactivity measurements were performed with a Lytle-designed in situ cell (17). A catalyst sample was pressed into a self-supporting wafer ∼150-μm thick to keep the vanadium absorbance ∼1. A small amount of unpressed catalyst was placed in the reactor next to and upstream of the wafer to enhance the MS detection of product stream maleic anhydride. This configuration satisfied the Weisz-Prater criterion (18) which ensures that the wafer and unpressed catalyst exhibited identical kinetics. The experiments were performed at the NSLS X6A beamline at Brookhaven National Laboratory. The x-ray optics were configured as described elsewhere (19) with the exception that a bent Si(111) crystal was used to access energies at the vanadium K-edge (5.46 keV). The data were analyzed with a variant of self-modeling curve resolution (20 21) the details of which will be published elsewhere (22). Briefly the data matrix ( D ) was factored into two subspaces related to the spectral characteristics ( S ) and composition profiles ( C ) that is D = SC. In our approach an initial estimate for C was projected into the composition subspace of the data to generate a new approximation to C using C = CUU † the constraint C ij > O was applied and iteration continued until the solution converged to a self-consistent set of concentration profiles and reference spectra. Singular value decomposition produced the matrix of significant right-hand eigenvectors U.
- Herron N. Thorn D. L. Harlow R. L. in preparation.
- Lytle F. W. The EXAFS Company Pioche NV 89043.
- Froment G. F., Bischoff K., Chemical Reactor Analysis and Design (Wiley, New York, 1979). / Chemical Reactor Analysis and Design by Froment G. F. (1979)
-
Lee P. L., et al., Rev. Sci. Instrum. 65, 1 (1994).
(
10.1063/1.1144778
) / Rev. Sci. Instrum. by Lee P. L. (1994) - Malinowski E. R., Factor Analysis in Chemistry (Wiley, New York, 1991). / Factor Analysis in Chemistry by Malinowski E. R. (1991)
-
Fernandez-Garcia M., Alvarez C. M., Haller G. L., J. Phys. Chem. 99, 12565 (1995).
(
10.1021/j100033a032
) / J. Phys. Chem. by Fernandez-Garcia M. (1995) - Coulston G. W. in preparation.
-
Wong J., Lytle F. W., Messmer R. P., Maylotte D. H., Phys. Rev. B 30, 5596 (1984).
(
10.1103/PhysRevB.30.5596
) / Phys. Rev. B by Wong J. (1984) - We gratefully acknowledge the assistance of G. Jenning who developed the beamline control software used in these experiments as well as J. Quintana for cutting the Si(111) crystal. This work was performed at the X6A beamline National Synchrotron Light Source Brookhaven National Laboratory which is supported by the Divisions of Materials Science and Chemical Science of the U.S. Department of Energy. Work at Northwestern was supported by the Division of Chemical Sciences of DOE.
Dates
Type | When |
---|---|
Created | 23 years, 1 month ago (July 27, 2002, 5:37 a.m.) |
Deposited | 1 year, 7 months ago (Jan. 13, 2024, 1:11 a.m.) |
Indexed | 1 month, 2 weeks ago (July 12, 2025, 6:49 p.m.) |
Issued | 28 years, 7 months ago (Jan. 10, 1997) |
Published | 28 years, 7 months ago (Jan. 10, 1997) |
Published Print | 28 years, 7 months ago (Jan. 10, 1997) |
@article{Coulston_1997, title={The Kinetic Significance of V 5+ in n -Butane Oxidation Catalyzed by Vanadium Phosphates}, volume={275}, ISSN={1095-9203}, url={http://dx.doi.org/10.1126/science.275.5297.191}, DOI={10.1126/science.275.5297.191}, number={5297}, journal={Science}, publisher={American Association for the Advancement of Science (AAAS)}, author={Coulston, George W. and Bare, Simon R. and Kung, Harold and Birkeland, Kari and Bethke, Gregory K. and Harlow, Richard and Herron, Norman and Lee, Peter L.}, year={1997}, month=jan, pages={191–193} }