Page 239 - Process Equipment and Plant Design Principles and Practices by Subhabrata Ray Gargi Das
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CHAPTER

                                                                                        9
               Phase equilibria














               9.1 Introduction
               Phase equilibrium data pertaining to the transferable component(s) is essential for design of any mass
               transfer process. Interphase mass transfer between immiscible phases occurs in the direction required
               to attain equilibrium, and its rate depends on the departure from equilibrium, i.e., how far away is the
               concentration of species i from the equilibrium concentration. Equilibrium concentration is inde-
               pendent of the amount/relative proportion of the two phases, and the locus of equilibrium concen-
               tration data generates the equilibrium distribution curve for each distributed component. The data can
               be presented either at constant temperature (isothermal data) or at constant pressure (isobaric data).
               Equilibrium distribution of the transferable component(s) represents the limiting composition(s) of the
               phases in each ideal stage of contact. The designer calculates the separation attainable in a mass
               transfer process consisting of one or more ideal contacting stages by estimating the equilibrium
               concentration(s) from phase equilibrium thermodynamics.
                  Generally speaking, whenever a dynamic equilibrium is established between phases, the con-
                                           centration of the species within individual phases (equilibrium
                                           concentration) is uniform and is fixed by the system temperature
                                           and pressure. In case of steady state, the species concentrations
                    Equilibrium and Steady State
                                           and the thermodynamic parameters (temperature, pressure, etc.)
                                           may not essentially be the same at all locations within a phase,
                                           but at every location, these do not vary with time. Hence, the
               equilibrium condition encompasses a steady-state condition, but the converse is not true.


               9.2 Representation of concentration
               The concentration of species i in a phase can have different representations. Usually, mole fraction or
               a quantity proportional to it, e.g., partial pressure of component in gas-liquid or gas-solid system is
               used to denote concentration in the gas phase. Traditionally the concentration of more volatile
               component in the liquid phase is x, and the same in vapor or another liquid phase richer in the
               component is denoted by y. In most situations, x and y denote mole fraction of the transferable
               species. Mole ratios X and Y maybeusedtorepresent molesof i per mole of phase free of component
               i,i.e., X ¼ x/(1   x) and Y ¼ y/(1   y).



               Process Equipment and Plant Design. https://doi.org/10.1016/B978-0-12-814885-3.00009-9  239
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