Chapter 2 Flashcards
energy requirements are determined by applying
the first law of thermodynamics
estimates of minimum energy needs can be made by
applying the second law of thermodynamics with an entropy balance or an availability balance
it is a measure of the maximum amount of energy that can be converted into shaft work
availability of a stream
loss of availability or exergy can be calculated in either of two ways
1 from the exergy (availability) balance
2 from the irreversible increase in the entropy of the universe
the equivalent work of separation for an irreversible process is given by
the sum of lost work and minimum work of separation
is the study of the equilibrium which exists between or within different states of matter namely solid, liquid, gas
phase equilibrium
is defined as a stage when chemical potential of any component present in the system stays steady with time
equilibrium
is a region where physical and chemical properties of the system are same throughout the region
phase
the distribution of phases in equilibrium is determined by application of
the gibbs free energy
is the starting point for the derivation of commonly used equations for expressing phase equilibria
gibbs free energy
at equilibrium, the total G for all phases is a minimum, and methods for determining this minimum are referred to as
free-energy minimization techniques
is the ratio of the partial fugacity of a component to its fugacity in a standard state, at a given temperature
activity
partial molar gibbs free energy of species i
μi, chemical potential
the chemical potential of a particular species in a multi-component system is _______ in all phases at physical equilibrium
identical
is employed as a surrogate for chemical potential as it is not a favored property for phase-equilibria calculations
fugacity
is a pseudo-pressure
partial fugacity
used to represent departure of activities from mole fractions when solutions are non-ideal
activity coefficient
is the ratio of mole fractions of a species in two phases in equilibrium
phase equilibrium ratio
For vapor-liquid (V-L) systems the phase equilibrium ratio is referred to as
K-value or vapor-liquid equilibrium ratio
for moderate pressures, the ______________ is introduced by approximating he pure-component liquid fugacity coefficient
poynting correction
is convenient for a low-molecular-weight gas species, whose temperature at the critical point is less than the system temperature
Henry’s law form for the k-value
for the liquid-liquid (L-L) systems the phase equilibrium ratio is referred to as
distribution or partition coefficient / liquid-liquid equilibrium ratio
is the ratio of equilibrium ratios
separation factor
for vapor-liquid systems, the separation factor is referred to as the
relative volatility