Bubble and dew point temperature calculations for a binary mixture. Isothermal and adiabatic flash calculations. Vapor and liquid enthalpy estimations for pure components and ideal mixtures.
Solution of systems of nonlinear algebraic equations.
Seader and Henley[1] (p. 171) investigated the process shown in Figure 12-1 where n-hexane (designated as component 1) is separated from n-octane by a series of three flash units at 1 atm. The feed to the first stage is an equimolar bubble point liquid at a flow rate of 100 kg-mol/h. The flash evaporator stages operate isothermally at the ...
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