“…Most often, its behavior is modeled after a Cross WLF model for the polymer viscosity with its different coefficients, for the PVT the coefficient of a two domain-Tait model, the transition temperature, T trans , value for the polymer, the shrinkage… Afterward, the data regarding the injection process have to be implemented with the melt polymer temperature, T Melt , the mold temperature, T Mo , the injection rate, the dynamic injected volume, the pressure and holding time, the cooling time, and the in-between cycle time. Lastly, the data regarding the mold with the mold/ polymer thermal exchange coefficient, h tc , for the different phases of the injection cycle, the precise dimensions of the cavity [4] and the runner system, the temperature and flow rate of the cooling fluid, and a perfect knowledge of cavity venting… All of these items will impact the simulation results to different degrees. A particularly sensitive point concerns the choice of the threshold value which allows the calculation to stop the flow of the polymer [9] in connection with the characteristics of the mold/ polymer heat exchanges.…”