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For a column with no side streams the fraction of the total feed flow going to the
                   overheads is given by:       FLOW-SHEETING                             187
                                                         x fk   x wk
                                               r overheads D
                                                         x dk   x wk
                   where x is the component composition and the suffixes f, d, w refer to feed, overheads
                   and bottoms respectively.

                   6. Equilibrium separators
                   This is a stream divider with two outlet streams, a and b, which may be considered to be
                   in equilibrium.


                                                                Stream a, x
                                         Feed                           ak
                                        x fk
                                                                Stream b, x bk
                   where x ak D concentration of component k in stream a,
                         x bk D concentration of component k in stream b,
                         x fk D concentration of component k in the feed stream.
                   If the equilibrium relationship can be expressed by a simple equilibrium constant, K k ,
                   such that:
                                                   x ak D K k x bk
                   Then the split-fraction coefficients can be calculated from a material balance.
                                                K k   x fk   x bk
                     Split fraction for stream a D            .
                                              K k   1   x fk


                                              4.7. REFERENCES
                   AUSTIN, D. G. (1979) Chemical Engineering Drawing Symbols (George Godwin).
                   BENEDEK, P. (ed.) (1980) Steady-state Flow-sheeting of Chemical Plants (Elsevier).
                   BS 1553: ... Specification for graphical symbols for general engineering
                     Part 1: 1977 Piping systems and plant.
                   COLBURN, A. P. (1939) Trans. Am. Inst. Chem. Eng. 35, 211. The simplified calculation of diffusional processes,
                       general considerations of two-film resistances.
                   CROWE,C. M., HAMIELEE,A. E.,HOFFMAN,T. N., JOHNSON,A.I., SHANNON,P.T. and WOODS, D. R. (1971)
                       Chemical Plant Simulation (Prentice-Hall).
                   DIN 28004 (1988) Flow sheets and diagrams of process plants, 4 parts (BSI).
                   GUNN, D. J. (1977) Inst. Chem. Eng., 4th Annual Research Meeting, Swansea, April. A sparse matrix technique
                       for the calculation of linear reactor-separator simulations of chemical plant.
                   GUNN, D. J. (1982) IChemE Symposium Series No. 74, 99, A versatile method of flow sheet analysis for process
                       evolution and modification.
                   HACHMUTH, K. H. (1952) Chem. Eng. Prog. 48 (Oct.) 523, (Nov.) 570, (Dec.) 570 (in three parts). Industrial
                       viewpoints on separation processes.
                   HENLEY, E.J.and ROSEN, E. M. (1969) Material and Energy Balance Computations (Wiley).
                   HUSAIN, A. (1986) Chemical Process Simulation (Wiley).
                   KREMSER, A. (1930) Nat. Petroleum News 22 (21 May) 43. Theoretical analysis of absorption columns.
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