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Useful-work bound from the Gibbs potential

Physical scope

Conditional finite endpoint bound for a closed fixed-composition system in the explicitly defined ideal constant-temperature, constant-pressure reservoir model; no claim is made that a reversible protocol exists or that the bound is attained.

Statement

For a fixed-composition closed system coupled to an ideal thermal reservoir at T0>0 and ideal pressure store at p0>0, let Q be heat into the system and let Wout be net energy delivered by the system to an ideal work store whose entropy is constant. Assume the isolated-composite model of [A1]–[A3] in Facts & Assumptions, including its admitted compound record, feasible endpoint association and admitted additive entropy split required by Macroscopic second law for isolated compounds. Then for any admitted process between equilibrium endpoints xi,xf,

Wout≤GT0,p0(xi)−GT0,p0(xf),GT0,p0(x):=U(x)+p0V(x)−T0S(x).

If the endpoint states lie on the (T,p)=(T0,p0) natural-variable chart, this is the decrease in the Gibbs potential of Local thermodynamic Legendre potentials. Equality requires zero total entropy production; the theorem does not assert that a protocol realizing equality exists.

Facts & Assumptions

Given: A system σ of fixed constitution c, an admitted record P∈Pcl(σ) with equilibrium endpoints xi,xf, T0>0, p0>0, and the ideal reservoir/work-store model below. The core-record conditions and fixed-chart bookkeeping are those of Thermodynamic process records and transfer conventions. Write Q=Q[P] and Won=Won[P]. Use Wout>0 for energy delivered by the system, in joules.

[A1]

Ideal thermal reservoir of constitution cR, with fixed volume and composition: its accessed equilibrium states have entropy SR(ER)=SR,0+ER/T0 on the accessed energy interval, where ER is its internal energy in joules and entropy is in J K−1. Heat Q into the system changes reservoir energy by ΔER=−Q.

[A2]

Ideal pressure and work stores: the only work on the system is Won=−p0ΔV−Wout, where the pressure store has energy change p0ΔV and the work store receives Wout. Both stores have constant entropy; no other work coordinate is admitted.

[A3]

The system, bath, and both stores form a compound C with an admitted record P^∈Pcl(C) representing the same operation as P. Its outer boundary is isolated throughout, its constitution is fixed, and its preparations at both endpoints are equilibrium macrostates. For both records the center-of-mass kinetic and separately tracked external-field energy changes vanish. Supply store endpoint sets YB,YW, energy maps EB:YB→R J and EW:YW→R J, and constant entropy maps SBaux:YB→R and SWaux:YW→R, with values in J K−1. The process model supplies ρP^:{−,+}→F⊆Dc×DcR×YB×YW with ρP^(−)=(xi,xR−,yB−,yW−) and ρP^(+)=(xf,xR+,yB+,yW+). The store-energy increments are exactly those in [A2]. Here F is one declared feasible constituent endpoint set for the fixed totals, retained constraints and permitted exchanges of [F2]; one fixed total-energy value on F is Uc(x)+UcR(xR)+EB(yB)+EW(yW), including both stores from [A2]. The system and bath form an independent separated split admitted by the entropy-additivity rule required in [F2]. Every named auxiliary and work device is included in C; any device outside this two-constituent entropy split has explicitly constant endpoint entropy. Thus Stot(x,xR,yB,yW)=Sc(x)+ScR(xR)+SBaux+SWaux on F gives ΔStot=ΔS+ΔSR.

[F1]

First-law energy balance for closed process records: The adopted closed-record balance is ΔU=Q+Won, with positive Q into and positive Won on the system.

[F2]

Macroscopic second law for isolated compounds: For an admitted core closed record of a compound isolated throughout, with fixed constitution and equilibrium endpoint tuples associated to the same declared feasible set, the entropy change of an admitted independent separated split is nonnegative. All named devices are included, omitted entropy contributions have declared zero change, and the kinetic and separately tracked external-field endpoint energy changes vanish.

[F3]

Thermodynamic process records and transfer conventions: Q and Won are process-record transfers, not state functions; an adiabatic record has Q=0.

[F4]

SI quantities and unit conventions: U, Q, and Won are in joules, V is in cubic metres, and Pa m3=J.

[F5]

Local thermodynamic Legendre potentials: On a valid local (T,p,n) inverse chart, the Gibbs potential is G=U−Ts+pV, with s the entropy coordinate.

Proof

1.1givenA1A2A3F1F2F3algebra

Apply [F1] to the system record P and use [A2] to obtain ΔU=Q−p0ΔV−Wout. By [A1] and [A3], ΔStot=ΔS−Q/T0. The compound record P^, its endpoint association into one F, and its admitted entropy split satisfy every hypothesis of [F2] by [A3], so ΔStot≥0 and Q≤T0ΔS. The signs of the transfers are those in [F3].

2.1givenA1A2F4F5step 1.1algebra∎

Rearranging step 1.1 gives Wout=−ΔGT0,p0−T0ΔStot≤−ΔGT0,p0. Since T0>0, equality implies ΔStot=0; no existence of an equality protocol follows. The units in [F4], the stated pressure and temperature units, and [A1]–[A2] make every energy term a value in joules. At endpoints with T=T0 and p=p0 on a valid Gibbs chart, [F5] equals GT0,p0, giving the stated Gibbs-potential interpretation.

Remarks

The result is a conditional model deduction. A finite reservoir, omitted shaft or field work, matter transfer, or an open-flow energy balance changes [A1]–[A3] and requires a separate argument.

Depends on

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