Page 21 - Distillation theory
P. 21

P1: FCH/FFX  P2: FCH/FFX  QC: FCH/FFX  T1: FCH
            CB644-FM   CB644-Petlyuk-v1                                                          June 15, 2004  4:28













                                Nomenclature
















                                A                        separation work
                                A                        stationary point of bond chain
                                A                        vertex of product simplex
                                B                        bottom stream (flow rate), kmol/sec
                                C (k)                    k-component boundary element of concentration
                                                           simplex
                                                         concentration simplex for n-component mixture
                                C n
                                d                        dimension of trajectory bundle
                                D                        overhead stream (flow rate), kmol/sec
                                E                        entrainer stream (flow rate), kmol/sec
                                F                        feed stream (flow rate), kmol/sec
                                h                        enthalpy of liquid, kJ/kg or kcal/kg
                                H                        enthalpy of vapor, kJ/kg or kcal/kg
                                h                        heave key component
                                i D : i B                split in column (i D and i B – components of
                                                           overhead and bottom products respectively)
                                i : j                    split in section (i and j present and absent
                                                           component of section product or pseudoproduct
                                                           respectively)
                                K                        equilibrium ratio
                                k                        number of product components at sharp
                                                           distillation
                                k                        key component
                                k                        key stationary point (pseudocomponent)
                                K ∞                      equilibrium ratio of component j at infinite dilution
                                 j
                                K t                      equilibrium ratio in tear-off point
                                l                        light key component
                                L                        liquid stream (flow rate), kmol/sec
                                m                        number of product components at sharp
                                                           distillation


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