Fourth Maxwell Relation
4. Fourth Maxwell Relation
By subtracting d(Ts) from both sides of Eq. (16) and using the relation g = h – Ts, we obtain the state equation
dg = v dP – s dT (24) where g represents the Gibbs function (named after Josiah Willard Gibbs, 1839–1903). Equa-
tion (24) is another form of the fundamental equation. The intensive form g (= g(T,P)) is also known as the chemical potential µ.
a. Remarks Since, dg = v(T,P) dP – s(T,P) dT,
( ∂g/∂T) P = –s(T,P) and ( ∂g/∂P) T = v(T,P) (25) so that
–ds = g TT dT + g TP dP and dv = g PT dT + g PP dP. The fourth Maxwell relation is represented by the equality ( ∂v/∂T) P = –( ∂s/∂P) T .
(26) The LHS of this expression is measurable while the RHS is not. Since s = –( ∂g/∂T) P ,
g = h – Ts = h + T ( ∂g/∂T) P or G = H + T ( ∂G/∂T) P . This relation is called the Gibbs–Helmholtz equation.
Furthermore, (
P – h/T –( ∂s/∂T) P = –h/T or( ∂(g/T)/∂(1/T)) P =h (27) Similarly from Eq. (24), ( ∂g/∂P) T = v.
∂(g/T)/∂T) 2 P =(
∂h/∂T) 2
(28) These relations are used to prove the Third law of thermodynamics and are useful in
chemical equilibrium relations. The phase change at a specified pressure (e.g., a piston containing an incompressible fluid with a weight placed on it) occurs at a fixed temperature. In that case, dP = dT =
0 and Eq. (24) implies that dg = 0, i.e., g f (for a saturated liquid) = g g (for saturated vapor at that pressure). Figure 3 illustrates the behavior of the properties h, s, and g when matter is heated from the solid to the liquid, and, finally, to the vapor phase.
Note the discontinuities regarding the entropy and Helmholtz function during the phase change, while g is continuous. At constant temperature, dg T = vdP. Therefore, the area under the v–P curve for an isotherm represents Gibbs function. The Planck function is represented by the relation
r = r(T,P) = –g/T = s – h/T, i.e.,
dr = – dg/T + g/T 2 dT = (1/T 2 )(- vT dP + h dT).
The relations for du, dh, da and dg can be easily memorized by using the phrase “Great Physicists Have Studied Under Very Articulate Teachers” (G, P, H, S, U, V,
A, T) by considering the mnemonic diagram (cf. Figure 4 ). In that figure a square is constructed by representing the four corners by the properties P, S, V, T, and by rep- resenting the property H by the space between the corners represented by P and S, the property U by the space between S and V, etc., as illustrated in Figure 4 . Diagonals are then drawn pointing away from the two bottom corners. Such a diagram is also known as a thermodynamic mnemonic diagram. If an expression for dG is desired (that is located at the middle of the line connecting the points T and P), we first form the differentials dT and dP, and then link the two with their conjugates as illustrated below dG = – S(the conjugate of T with the minus sign due to the diagonal pointing towards T) × dT + V (that is conjugate of P with the plus sign due to the diagonal pointing
away from P) × dP.
Parts
» COMPUTATIONAL MECHANICS and APPLIED ANALYSIS
» Explicit and Implicit Functions and Total Differentiation
» Exact (Perfect) and Inexact (Imperfect) Differentials
» Intermolecular Forces and Potential Energy
» Internal Energy, Temperature, Collision Number and Mean Free Path
» Vector or Cross Product r The area A due to a vector product
» First Law for a Closed System
» First Law For an Open System
» STATEMENTS OF THE SECOND LAW
» Cyclical Integral for a Reversible Heat Engine
» Irreversibility and Entropy of an Isolated System
» Degradation and Quality of Energy
» SINGLE–COMPONENT INCOMPRESSIBLE FLUIDS
» Evaluation of Entropy for a Control Volume
» Internally Reversible Work for an Open System
» MAXIMUM ENTROPY AND MINIMUM ENERGY
» Generalized Derivation for a Single Phase
» LaGrange Multiplier Method for Equilibrium
» Absolute and Relative Availability Under Interactions with Ambient
» Irreversibility or Lost Work
» Applications of the Availability Balance Equation
» Closed System (Non–Flow Systems)
» Heat Pumps and Refrigerators
» Work Producing and Consumption Devices
» Graphical Illustration of Lost, Isentropic, and Optimum Work
» Flow Processes or Heat Exchangers
» CLASSICAL RATIONALE FOR POSTULATORY APPROACH
» Generalized Legendre Transform
» Van der Waals (VW) Equation of State
» Other Two–Parameter Equations of State
» Compressibility Charts (Principle of Corresponding States)
» Boyle Temperature and Boyle Curves
» Three Parameter Equations of State
» Empirical Equations Of State
» State Equations for Liquids/Solids
» Internal Energy (du) Relation
» EXPERIMENTS TO MEASURE (u O – u)
» Vapor Pressure and the Clapeyron Equation
» Saturation Relations with Surface Tension Effects
» Temperature Change During Throttling
» Throttling in Closed Systems
» Procedure for Determining Thermodynamic Properties
» Euler and Gibbs–Duhem Equations
» Relationship Between Molal and Pure Properties
» Relations between Partial Molal and Pure Properties
» Mixing Rules for Equations of State
» Partial Molal Properties Using Mixture State Equations
» Ideal Solution and Raoult’s Law
» Completely Miscible Mixtures
» DEVIATIONS FROM RAOULT’S LAW
» Mathematical Criterion for Stability
» APPLICATION TO BOILING AND CONDENSATION
» Physical Processes and Stability
» Constant Temperature and Volume
» Equivalence Ratio, Stoichiometric Ratio
» Entropy, Gibbs Function, and Gibbs Function of Formation
» Entropy Generated During an Adiabatic Chemical Reaction
» MASS CONSERVATION AND MOLE BALANCE EQUATIONS
» Evaluation of Properties During an Irreversible Chemical Reaction
» Criteria in Terms of Chemical Force Potential
» Generalized Relation for the Chemical Potential
» Nonideal Mixtures and Solutions
» Gas, Liquid and Solid Mixtures
» Availability Balance Equation
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