A process for preparing a propane oxidation catalyst, the process comprising pre-calcining a catalyst precursor in a precalcining zone in an oxygen-containing gas, then feeding an oxygen-free gas to a purging zone until the gas exiting the zone is substantially free of oxygen, and calcining the pre-
A process for preparing a propane oxidation catalyst, the process comprising pre-calcining a catalyst precursor in a precalcining zone in an oxygen-containing gas, then feeding an oxygen-free gas to a purging zone until the gas exiting the zone is substantially free of oxygen, and calcining the pre-calcined precursor to obtain the catalyst.
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1. A process for preparing a propane oxidation catalyst, the process comprising: (a) preparing a catalyst precursor; (b) pre-calcining the catalyst precursor in a precalcining zone in an oxygen-containing gas at a temperature of less than 330° C. to form a pre-calcined precursor; then (c) feeding an
1. A process for preparing a propane oxidation catalyst, the process comprising: (a) preparing a catalyst precursor; (b) pre-calcining the catalyst precursor in a precalcining zone in an oxygen-containing gas at a temperature of less than 330° C. to form a pre-calcined precursor; then (c) feeding an oxygen-free gas to the pre-calcined precursor in a purging zone until the gas exiting the purging zone is substantially free of oxygen, wherein the temperature of the purging zone is less than 330° C., and (d) calcining the pre-calcined precursor to obtain the catalyst. 2. The process of claim 1 wherein the catalyst comprises less than 4% of M5O14 phase. 3. The process of claim 1 wherein the catalyst comprises less than 2% of M5O14 phase. 4. The process of claim 1 wherein the oxygen-free gas comprises primarily nitrogen. 5. The process of claim 1 wherein the temperature of at least one of the precalcining zone or the purging zone is less than 310° C. 6. The process of claim 1 wherein the temperature of at least one of the precalcining zone or the purging zone is less than 290° C. 7. The process of claim 1 wherein the temperature of at least one of the precalcining zone or the purging zone is less than 280° C. 8. The process of claim 1 wherein step (b) is continued until the weight of the precursor stabilizes to obtain a pre-calcined precursor. 9. The process of claim 1 wherein the catalyst is represented by the formula AaVbNcXdZeOf wherein A is at least one element selected from the group consisting of Mo and W, N is at least one element selected from the group consisting of Te and Sb, X is at least one element selected from the group consisting of Nb, Ta, Ti, Al, Zr, Cr, Mn, Fe, Ru, Co, Rh, Ni, Pt, Sb, Bi, B, In, As, Ge, Sn, Hf, Pb, P, Pm, Eu, Gd, Dy, Ho, Er, Tm, Yb and Lu, and Z is at least one element selected from the group consisting of Zn, Ga, Ir, Sm, Pd, Au, Ag, Cu, Sc, Y, Pr, Nd and Tb; and wherein, when a=1, b=0.01 to 1.0, c=0.01 to 1.0, d=0.01 to 1.0, e=0 to 0.1 and f is dependent on the oxidation state of the other elements. 10. The process of claim 1 wherein A=Mo, N=Te, and X=Nb.
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