Thermodynamics Flashcards
(84 cards)
mole fraction
mole fraction of component J
amount of J (in moles) divided by the total moles, n of molecules in the mixture
partial molar volume
partial molar volume of component J in a mixture
change in volume per mole of J added to a large volume of the mixture
V𝐽 is the tangent (derivative) of the curve describing the total
volume, V of the mixture as a function of the amount of J (in moles)
at constant p, T and amount 𝑛𝑖≠𝐽 of any other component in the mixture
change in the total volume V of a mixture due to the addition of
small amounts of A and small amounts of B
V is a state function, only depends on the composition of the mixture.
equation can be used independently of how nA and nB are mixed
partial molar volume varies with mixture composition
when composition is altered, the environment experienced by each component (and its interaction with the other components) changes
also varies with p and T
extensive property
any property (mass, volume) that depends on the absolute amount of matter
intensive property
any property (partial molar quantity/volume, density) that depends on the amount of matter normalised to the sample size
partial molar Gibbs energy (chemical potential)
the tangent (derivative) of the curve describing the Gibbs energy as a function of the amount of J (in moles)
at constant p, T and amount 𝑛𝑖≠𝐽 of any other component in the mixture.
Gibbs energy for binary mixture
fundamental equation of chemical thermodynamics (modified to account for changes in composition)
chemical potential changes with changes to p, T and composition
new term accounts for any additional non-expansion work that the system can
perform due to changes of its composition (changes in 𝑛𝐽)
as a consequence of phase changes/chemical reactions
modified equation for binary mixtures
Gibbs energy of mixing: the case of ideas gases
gas A and gas B initially occupy different compartments of a container - separated by a partition
their chemical potentials is the molar Gibbs energy of the pure substances, μ = Gm.
μ(p) - chemical potential of an ideal gas
Gibbs energy before mixing
Gibbs energy after mixing
after the partition is removed
p = pA + pB
pA and pB = gases’ partial pressures in the mixture
Gibbs energy of mixing
Gibbs energy of mixing in terms of mole fraction
𝑥𝐽 is always <1
hence, ln 𝑥𝐽 < 0 so that ∆mixG < 0 (always negative) for all compositions
confirms that mixing ideal gases is always a spontaneous process at any composition
entropy of mixing
ln x < 0, ∆mixS > 0 (always positive) for all compositions
mixing gases increases disorder, greater entropy
enthalpy of mixing
Using ∆G = ∆H −T∆S,
we obtain that ∆mixH = 0 for all compositions
(i.e. no interaction exist between molecules of ideal gases).
enthalpy in the system constant, therefore the increase in entropy is what drives the mixing of two ideal gases.
Gibbs energy (left) and entropy of mixing (right) of two ideal gases
When the liquid and gas phases of pure A are at equilibrium, the chemical potentials of the two phases are identical
When the liquid phase also contains solute B, the criterion of phase equilibrium still holds for A
combine equations for 𝝁𝑨* and 𝝁𝑨
Raoult’s law
partial vapour pressure, pA
mole fraction, 𝑥A
vapour pressure of pure A, pA*
physical interpretation of Raoult’s law
when there is solute B, the rate at which the solvent A evaporates decreases without altering the rate at which it condenses to the liquid phase from the gas phase
solute molecules (small, black) prevent solvent molecules (large, blue) at the surface of a solution to pass into the gas phase (dashed arrow) but not the opposite exchange (solid arrows).
rates of vaporization and
condensation for A
Vapourisation rate = kxA
Condensation rate = k′pA
k and k′ are proportionality constants