Numerical calculation of chemical-technological system reactor-distillation column is done. The reaction takes place in the continuous stirred tank reactor. Numerical calculations proved, that continuum of the steady states exists for the regimes with the full using of basic reactants. It is displayed as a dependence of calculated concentrations of the reactants in the reactor on the initial values of iteration procedure.
химико-технологическая система, реактор - ректификационная колонна, множественность стационарных состояний, реактор с рециклом, reactor with recycle, multiplicity of steady states, chemical-technological system, reactor-distillation column
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