Applicability of three models for rector simulation at different levels of details is investigated, from the viewpoint of design of dynamic operation to perform the unsteady operation for dealing with the catalyst deterioration and the emergency stopping operation safely and efficiently. In this study, we develop three simulation systems by combining the standard unit models in the Visual Modeler, which are the fixed bed reactor model, the heat exchanger model and so on, in order to investigate influence of the number of spatial divisions of the model on dynamic simulation results. Then, methods for extension of submodels concerned with the reaction and the heat transport phenomena are developed by considering the catalyst deterioration and the phase change of coolant. When three case studies for load down in the vinyl acetate monomer process are performed by the developed simulation systems, application of a simulation method of expressing the divided heat transfer wall by a series of heat exchanger models is demonstrated to be useful for examination of dynamic operation by comparing with the conventional simulation method that is described in the previous paper.