Group
contribution (GC) approaches are based on the premise that
the properties of a molecule or a mixture can be determined from the
appropriate contributions of the functional chemical groups present
in the system of interest. Although this is clearly an approximation, GC methods
can provide accurate estimates of the properties of many systems and
are often used as predictive tools when experimental data are scarce
or not available. Our focus is on the SAFT-γ Mie approach [Papaioannou,
V.; Lafitte, T.; Avendaño, C.; Adjiman, C. S.; Jackson, G.; Müller,
E. A.; Galindo, A. Group contribution methodology based on the statistical
associating fluid theory for heteronuclear molecules formed from Mie
segments. J. Chem. Phys.
2014, 140, 054107–29] which incorporates a detailed heteronuclear
molecular model specifically designed for use as a GC thermodynamic
platform. It is based on a formulation of the recent statistical associating
fluid theory for Mie potentials of variable range, where a formal
statistical–mechanical perturbation theory is used to maintain
a firm link between the molecular model and the macroscopic thermodynamic
properties. Here we summarize the current status of the SAFT-γ
Mie approach, presenting a compilation of the parameters for all functional
groups developed to date and a number of new groups. Examples of the
capability of the GC method in describing experimental data accurately are provided,
both as a correlative and as a predictive tool for the phase behavior
and the thermodynamic properties of a broad range of complex fluids.
A three-step sintering mechanism is proposed for Co-based
catalysts
under Fischer–Tropsch reaction conditions. This mechanism includes
an intermediate formation of oxide layer on cobalt metal nanoparticles
in the presence of water. The partially reversibly oxidized surface
accelerates sintering by both reducing the surface energy and enhancing
the diffusion rates of cobalt particles. The proposed mechanism is
then employed for a fixed-bed unsteady state reactor. The effect of
particle growth on the catalytic activity was analyzed within a diverse
range of operating conditions (syngas ratio = 1.5–4, water
co-feed ratio = 0–6, inert co-feed ratio = 0–6). It
is found that, at the same gas space velocity, sintering proceeds
faster at higher H2/CO ratios. At the same initial conversion,
a low H2/CO syngas ratio increases sintering severity,
i.e., catalyst deactivation due to the crystallite growth, as it brings
about higher relative water partial pressure. Dilution of syngas with
different amounts of inert gas does not affect the cobalt sintering
rate. Cobalt sintering proceeds more rapidly if water is co-fed during
the reaction.
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