“…For instance, Dammers and Tels (1974), based on the Brussels school of thermodynamics (Glansdorff and Prigogine, 1971), proposed a suitable potential function related to Prigogine's velocity potential to state a stability criteria in adiabatic stirred flow reactors, and Tarbell (1977) has proposed a Lyapunov function for continuous stirred tank reactor (CSTR) with a steady state near the equilibrium point, that resembled the thermodynamical entropy production function, while Georgakis (1986) suggested the use of extensive rather than intensive variables for process control purposes. More recently, Alonso, Ydstie and coworkers have explored this research area, that resulted in very insightful works on the control design of process ssystems (see e.g., Ydstie, 1996, 2001;Ydstie and Alonso, 1997;Coffey et al, 2000;Alonso et al, 2002;Ydstie, 2002;Balaji et al, 2010) to develop stabilizing mass and energy inventory controllers (Farschman et al, 1998) and to derive general structural stability conditions for chemical process networks (Hangos et al, 1999;Antelo et al, 2007;Baldea et al, 2013;Hioe et al, 2013). In addition to the concept of inventories, they have used a nonlinear extension of the curvature of the entropy function called availability as it has been proposed within the framework of passivity theory for processes.…”