“…The thermal equilibrium parameters can be monitored and controlled by the maturely developed probes for O 2 , H 2 O, and CO 2 , and thermal couples, while the kinetic parameters should be designed based on the properties of the steels and the interactions on the steel/gas interface. By linear non-equilibrium thermodynamics, the kinetics of carburizing is governing by the so-called duration of carbon potential build-up (τ CP , s), the surface transfer coefficient of carbon (β, cm•s −1 ), and the bulk diffusion coefficient of carbon (D, cm 2 •s −1 ). It is usually pre-assumed that the build-up of carbon potential is relatively fast by rational design of convective flow of gases, Coatings 2022, 12, 1886 2 of 14 while the surface transfer and bulk diffusion of carbon are considered as the rate-limiting steps [2][3][4][5][6].…”