A third kind of kinetics which is termed bed lumped kinetics is propos
ed. According to its implicate, all the catalysts contained in a singl
e-tube reactor are treated as a whole, which is like a large cylindric
al pellet. In this manner, the proposed kinetics can be in a much larg
er space scale than those of the intrinsic kinetics and particle appar
ent kinetics. Bed lumped kinetics is obtained under actual industrial
operating conditions. Therefore the reliability of the model parameter
s can be greatly improved, and it can reduce the uncertainties in extr
apolation and will be more suitable in the modeling of a fixed-bed rea
ctor. The calculation of the confidence region and correlation matrix
of the parameters under different experimental conditions proves that
bed lumped kinetics is a concept for the fixed-bed reactors with both
theoretically tenable and practically achievable properties.