Chapter 2 Flashcards

1
Q

energy requirements are determined by applying

A

the first law of thermodynamics

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2
Q

estimates of minimum energy needs can be made by

A

applying the second law of thermodynamics with an entropy balance or an availability balance

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3
Q

it is a measure of the maximum amount of energy that can be converted into shaft work

A

availability of a stream

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4
Q

loss of availability or exergy can be calculated in either of two ways

A

1 from the exergy (availability) balance
2 from the irreversible increase in the entropy of the universe

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5
Q

the equivalent work of separation for an irreversible process is given by

A

the sum of lost work and minimum work of separation

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6
Q

is the study of the equilibrium which exists between or within different states of matter namely solid, liquid, gas

A

phase equilibrium

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7
Q

is defined as a stage when chemical potential of any component present in the system stays steady with time

A

equilibrium

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8
Q

is a region where physical and chemical properties of the system are same throughout the region

A

phase

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9
Q

the distribution of phases in equilibrium is determined by application of

A

the gibbs free energy

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10
Q

is the starting point for the derivation of commonly used equations for expressing phase equilibria

A

gibbs free energy

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11
Q

at equilibrium, the total G for all phases is a minimum, and methods for determining this minimum are referred to as

A

free-energy minimization techniques

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12
Q

is the ratio of the partial fugacity of a component to its fugacity in a standard state, at a given temperature

A

activity

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13
Q

partial molar gibbs free energy of species i

A

μi, chemical potential

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14
Q

the chemical potential of a particular species in a multi-component system is _______ in all phases at physical equilibrium

A

identical

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15
Q

is employed as a surrogate for chemical potential as it is not a favored property for phase-equilibria calculations

A

fugacity

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16
Q

is a pseudo-pressure

A

partial fugacity

17
Q

used to represent departure of activities from mole fractions when solutions are non-ideal

A

activity coefficient

18
Q

is the ratio of mole fractions of a species in two phases in equilibrium

A

phase equilibrium ratio

19
Q

For vapor-liquid (V-L) systems the phase equilibrium ratio is referred to as

A

K-value or vapor-liquid equilibrium ratio

20
Q

for moderate pressures, the ______________ is introduced by approximating he pure-component liquid fugacity coefficient

A

poynting correction

21
Q

is convenient for a low-molecular-weight gas species, whose temperature at the critical point is less than the system temperature

A

Henry’s law form for the k-value

22
Q

for the liquid-liquid (L-L) systems the phase equilibrium ratio is referred to as

A

distribution or partition coefficient / liquid-liquid equilibrium ratio

23
Q

is the ratio of equilibrium ratios

A

separation factor

24
Q

for vapor-liquid systems, the separation factor is referred to as the

A

relative volatility

25
for liquid-liquid systems, the separation factor is referred to as the
relative selectivity
26
where does the simplest (EOS) model apply
when both liquid and vapor phases are ideal solutions (all activity coefficients equal to 1.0) and the vapor is an ideal gas
27
is expressed in terms of vapor-liquid and liquid-liquid K-values, which are formulated in terms of fugacity coefficients and activity coefficients
phase equilibrium
28