Erratum to “Hydrodynamic simulation of gas–solids downflow reactors” [Chem. Eng. Sci. 63 (2008) 5107–5119]

Numerical evaluation on the intraparticle transfer in butylene oxidative dehydrogenation fixed-bed reactor over ferrite catalysts

“…The PMM is used to describe the gas-solid flow in the fixed-bed reactor, and the SPM is used to represent the intraparticle transfer and reaction. These models are briefly summarized in Tables 1 and 2 [22][23][24][25][26][27][28]. The average gas velocity is approximately 0.033 m/s in the porous medium, and the numerical Re number is close to 6.…”