A process for preparing a propane oxidation catalyst, the process comprising pre-calcining the catalyst precursor in an oxygen-containing gas at a temperature of less than 330° C. until the weight of the precursor stabilizes to obtain a pre-calcined precursor; then calcining the pre-calcined precurs
A process for preparing a propane oxidation catalyst, the process comprising pre-calcining the catalyst precursor in an oxygen-containing gas at a temperature of less than 330° C. until the weight of the precursor stabilizes to obtain a pre-calcined precursor; then 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 an oxygen-containing gas at a temperature of less than 330° C. until the weight of the precursor stabilizes to obtain a pre-calcined precur
1. A process for preparing a propane oxidation catalyst, the process comprising: (a) preparing a catalyst precursor; (b) pre-calcining the catalyst precursor in an oxygen-containing gas at a temperature of less than 330° C. until the weight of the precursor stabilizes to obtain a pre-calcined precursor; then (c) calcining the pre-calcined precursor to obtain the catalyst, wherein step (b) is maintained for at least 5 hours, and wherein the catalyst comprises an orthorhombic phase M1 and a pseudo-hexagonal phase M2, and wherein the amount of phase M2 in the catalyst is less than 12%. 2. The process of claim 1 wherein step (b) is maintained for at least 6 hours. 3. The process of claim 1 wherein step (b) is maintained for at least 8 hours. 4. The process of claim 1, wherein the amount of phase M2 in the catalyst is less than 10%. 5. The process of claim 1, wherein the amount of phase M2 in the catalyst is less than 8%. 6. The process of claim 1, wherein the amount of phase M2 in the catalyst is less than 7%. 7. The process of claim 1, wherein the temperature of step (b) is less than 310° C. 8. 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. 9. The process of claim 1, wherein A=Mo, N═Te, and X═Nb.
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