Prelim Flashcards

1
Q

The total Gibbs Free Energy for all phases in a multiphase, multicomponent system is

A

Minimum

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2
Q

The ratio of mole fractions of a species present in liquid-liquid equilibrium

A

distribution coefficient

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3
Q

For non ideal liquid solutions the model for correlating liquid-phase activity coefficients of binary pairs that uses local area fraction as the primary concentration variable rather than local volume or mole fractions

A

UNIQUAC

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4
Q

A solution is ideal when activity coefficients are all equal to

A

1

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5
Q

Fugacity as a substitute for chemical potential in phase equilibria calculations was proposed by

A

Lewis

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6
Q

For systems in equilibrium, the given species in each existing phase has equality of phase

A

chemical potential

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7
Q

Graphical correlations of pure component thermodynamic properties are widely available for an solution at near

A

Ambient Pressure

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8
Q

The approximate expression for estimating K-value for non ideal liquid solutions at moderate pressure and below the critical temperature

A

Poynting correction

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9
Q

The ratio for the equilibrium ratios for vapor-liquid systems is the

A

Relative Volatility

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10
Q

For a pure ideal gas, fugacity is equal to

A

Pressure

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11
Q

Equation that provides the quantitative measure of the thermodynamic inefficiency of the process

A

Availability Balance

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12
Q

Dissolving pharmaceutical products from bark or roots of plants employs

A

Leaching

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13
Q

For non ideal vapor and liquid mixtures containing non polar components which of the following equations can be used to estimate activity coefficients, volume and Enthalpy of mixing and K values

A

SR
PR
LKP
So All of these

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14
Q

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

A

Lost work + Minimum work

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15
Q

Which of the following describes activity

A

ratio of partial fugacity of a component to its fugacity in some defined standard state

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16
Q

Which of the following equations of state for non ide vapor and liquid mixtures does not use acentric factor

A

Redlich-Kwong

17
Q

For a pure ideal gas, fugacity equals

A

Total Pressure

18
Q

Which is true about lost work in a separation operation

A

the greater its value the greater the energy inefficiency

19
Q

The simplest model of when both vapor and liquid are ideal solutions and the vapor is an ideal gas applies only at near ambient pressure up to about

A

50 psia

20
Q

Which is not true about availability

A

is conserved in a real irreversible process

21
Q

Fick’s law of Diffusion is an extension of

A

Fourier’s Law of heat conduction

22
Q

Which of the following is not true about binary equimolar counterdiffusion

A

at constant molar density Dab = - Dba

23
Q

For equimolar mixture of A and B, in unimolecular diffusion, mass transfer of component A in stagnant B, if 1 - Xa is 0.5, then

A

NA = 2JA

24
Q

For estimating the diffusivity in gas mixtures, which of the following equations can be used

A

Chapman-Enskog Equation

25
Q

The Nernst-Haskell equation is used to estimating diffusion coefficients of

A

electrolytes

26
Q

For steady state, one dimensional molecular diffusion through stationary medium B, with constant DAB, the molar rate of mass transfer of A for plane wall is proportional to, EXCEPT

A

thickness
( it is proportional to diffusivity, area, and concentration gradient)

27
Q

The model for mass transfer at fluid-fluid interface most useful when mass transer involves bubbles or droplets or flow over random packing

A

Penetration theory

28
Q

The total molar rate of absorption of A through a falling liquid film B is directly proportional to

A

film thickness
film width
concentration gradient

29
Q

The mass transfer coefficient for component A is given by

A

kc = nA/A∆CA

30
Q

Used to estimate the values of heat and mass transfer coefficients from experimental measurements of the Fanning friction factor for turbulent flow at Npy= Nsc= 1

A

Reynolds Analogy