Catalytic performance of multicomponent bismuth molybdates (Ni Fe3Bi1Mo12O42+) in the oxidative dehydrogenation of C4 raffinate-3 to 1,3-butadiene: Effect of nickel content and acid property

Abstract

Abstract Multicomponent bismuth molybdate (Ni X Fe 3 Bi 1 Mo 12 O 42+ X ) catalysts were prepared by a co-precipitation method with a variation of nickel content, and were applied to the oxidative dehydrogenation of C 4 raffinate-3 to 1,3-butadiene. Conversion of n -butene and selectivity for 1,3-butadiene over Ni X Fe 3 Bi 1 Mo 12 O 42+ X catalysts showed volcano-shaped curves with respect to nickel content. As a consequence, yield for 1,3-butadiene also showed a volcano-shaped curve with respect to nickel content. Among the catalysts tested, Ni 9 Fe 3 Bi 1 Mo 12 O 51 showed the best catalytic performance. Acid properties of Ni X Fe 3 Bi 1 Mo 12 O 42+ X catalysts were measured by NH 3 -TPD experiments, with the aim of correlating the catalytic performance with the acid property of the catalysts. It was observed that either total acidity or acid strength was not directly correlated with the catalytic performance of Ni X Fe 3 Bi 1 Mo 12 O 42+ X catalysts. However, the conversion of n -butene was increased with increasing surface acidity of the catalyst. The largest surface acidity of the Ni 9 Fe 3 Bi 1 Mo 12 O 51 catalyst was responsible for its enhanced catalytic performance in the oxidative dehydrogenation of C 4 raffinate-3. The facile oxygen mobility of the γ-Bi 2 MoO 6 phase in the Ni 9 Fe 3 Bi 1 Mo 12 O 51 catalyst also played an important role in enhancing the catalytic performance of the Ni 9 Fe 3 Bi 1 Mo 12 O 51 catalyst.