| US 7,576,232 B2 | ||
| In situ modification of molybdenum-based catalysts | ||
| Michael J. Seely, Naperville, Ill. (US); and Christos Paparizos, Willoughby, Ohio (US) | ||
| Assigned to Ineos USA LLC, Lisle, Ill. (US) | ||
| Filed on May 02, 2006, as Appl. No. 11/415,565. | ||
| Prior Publication US 2007/0260085 A1, Nov. 08, 2007 | ||
| Int. Cl. C07C 253/00 (2006.01) | ||
| U.S. Cl. 558—321 | 13 Claims |
| 1. A process for the conversion of a hydrocarbon selected from the group consisting of propylene, isobutylene, propane, isobutane
or mixtures thereof, to acrylonitrile, methacrylonitrile, or mixtures thereof, the process comprising contacting in a reactor
and reacting in the vapor phase at an elevated temperature and pressure said hydrocarbon with a molecular oxygen-containing
gas and ammonia, in the presence of a molybdenum-based ammoxidation catalyst and a catalyst modifier, wherein said molybdenum-based
ammoxidation catalyst comprises an oxide represented by the following formula:
AaBbCcDdBieMofOx where
A is one or more of Li, Na, K, Cs, Rb, Sm, In, Ca, Sr, Ba and Tl,
B is one or more of Fe, Co, Mg, Mn, Ni, V and Zn,
C is one or more of Cr, Ce, Eu, P, Sb, Ge, Te and W,
D is one or more of Sn, B, As, Pt, Pd, Ga, Nd, Nb, Pr and Pb, and
a is 0.05 to 3.0,
b is 0.1 to 14.0,
c is 0.0 to 5.0,
d is 0.0 to 2.0,
e is 0.2 to 6.0,
f is 8.0 to 18.0,
and x is a number determined by the oxidation states and amounts of the other elements present in the catalyst (i.e. x a number
determined by the valence requirements of the other elements present); and
wherein said catalyst modifier comprises a molybdate or a polymolybdate of at least one element M selected from the group
consisting of cesium, rubidium, potassium, sodium, thallium, lithium, nickel, cobalt, iron, chromium, copper, magnesium, manganese,
cerium and phosphorus.
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