Page 377 - Chemical process engineering design and economics
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356                                                      Chapter 6

            g       acceleration of gravity

            H       height

                    dispersion zone thickness
            H D
            HETS    height equivalent to a theoretical stage

            JT      total volumetric flow rate per unit area

            k       flooding  factor

                    entrainment factor
            k v
            K       liquid-vapor or liquid-liquid equilibrium ratio

            L       length

                    the length of the dispersion layer
            L D
            LS      length of the lower section of a column, or decanter length required
                    for the dispersed phase to settle

            m       mass or molar flow rate

            m D     mass of dry cake

                    mass flow rate of liquid, molar flow rate, or mass of a liquid drop
            m L
            ms      mass of dry filter  cake

            m       vapor mass flow rate or molar flow rate

            ML      molecular weight of a liquid


            M v     molecular weight of a vapor
            n ; B   number of moles of component i in the bottoms

                    number of moles of  component i in the distillate
            n iD
           NA       number of actual stages

                    number of equilibrium stages
           N e


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