Modelling of the CSTR seems fairly straight forward, using e.g. Excel, Matlab or Scilab and a simple equation solver to solve for the reaction extents for which the reaction rates match the kinetic expression.
Modelling of the Gibbs reactor requires inclusion of a Gibbs term for carbon. The remaining terms can simply be obtained from G = H - T * S where H = enthalpyF and S is entropyF. Also this can be done in Excel, Matlab or Scilab, using a multi-dimensional minimization (e.g. modify reaction extents so that total Gibbs energy is minimized).Statistics: Posted by jasper — 05 November 2018, 08:46
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