A method to calculate multi-component chemical reaction mixtures as a
sequence of time-dependent, intermediate thermochemical states is pres
ented. The method combines the: overall reaction kinetics with thermod
ynamic Gibbs energy minimization, The overall reaction is assumed to p
roceed according to the Arrhenius rate law. During the time-course of
the reaction, the temperature;md composition of the reaction mixture a
re calculated by a thermodynamic subroutine, which minimizes the Gibbs
energy of the system, The extent of the overall reaction is algorithm
ically constrained in the Gibbs energy minimization procedure, During
the sequential calculation, the kinetic condition is removed by finite
differences, The temperature of each intermediate state is reached by
an iterative procedure, which takes into acconnt the heat transfer be
tween the system and its surroundings and the enthalpy changes due to
the chemical reactions, Thus, the method allows for the effect of temp
erature on the reaction kinetics as the reaction evolves. The chemical
species present in each intermediate state are virtually independent
and there is a chemical potential assigned to each of these species. T
he gradual chemical change in the thermodynamic system proceeds from t
he initial state of mixed reactants to the final state of product mixt
ure, Both stationary and transient phenomena may be calculated, The me
thod has been applied to some well-known industrial multi-component re
action systems and a fair agreement between the calculated and measure
d values has been obtained. The application of the thermochemical algo
rithm in reaction calorimetry is discussed. (C) 1997 Elsevier Science
B.V.