A NNALES DE L ’I. H. P., SECTION A
A. P AGLIETTI
The mathematical formulation of the local form of the second principle of thermodynamics
Annales de l’I. H. P., section A, tome 27, n
o2 (1977), p. 207-219
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207
The mathematical formulation of the local form of the second principle of thermodynamics
A. PAGLIETTI
Mathematical Institute, University of Oxford
Vol. XXVII, n° 2, 1977, Physique théorique.
ABSTRACT. - The aim of this paper is to demonstrate that the so-called Clausius-Planck
inequality
represents the correct local formulation of the secondprinciple
ofthermodynamics
forsingle-phase
continuous materials.A
precise meaning
is attributed to theconcepts
of state,reversibility, equilibrium
process, etc., and the notion ofentropy
is defined both forequilibrium
andnon-equilibrium
processes. Theanalysis
shows that the Clausius-Planckinequality
must be valid ingeneral
fornon-equilibrium/
non-homogeneous
processesprovided,
of course, that amacroscopic
des-cription
of the process ispossible.
RESUME. - Le but de cet article est de démontrer que
l’inégalité
deClausius-Planck
représente
la formulation locale correcte du deuxiemeprincipe
de lathermodynamique
pour le casclassique
de materiaux continusayant
unephase unique.
On attribue un sensprecis
auxconcepts d’etat,
de
réversibilité,
de processusd’équilibre,
etc., et on dennit la notion d’entro-pie
pour les processusd’équilibre
et pour les processus au dehors de1’equi-
libre. On démontre que
I’inégalité
de Clausius-Planck doit êtrevalide,
en
general,
pour processus au dehorsd’équilibre
et pour processus nonhomogènes,
pourvu que,naturellement,
il soitpossible
de décrire cesprocessus d’un
point
de vuemacroscopique.
1. INTRODUCTION
Local forms of the second
principle
ofthermodynamics
are often intro-duced in continuum mechanics as mathematical
generalizations
of wellAnnales de l’Institut Henri Poincare - Section A - Vol. XXVII, n° 2 - 1977.
208 A. PAGLIETTI
established formulae of classical
thermodynamics.
Of course, when thesegeneralizations
arepursued
in an abstract waythey
may lead to relations which do notrespect
theoriginal
content of the secondprinciple : impossi- bility
ofperpetual
motion of the second kind(cf. [4], ~ 106-136).
Seriousdoubts in this sense have been
recently
raised(cf. [8])
for the so-calledlocal form of the Clausius-Duhem
inequality.
The aim of thepresent
articleis to deduce for
single-phase
continuous materials ananalytical
local condi-tion which is both necessary and suflicient to exclude the occurrence of
perpetual
motions of the second kind. Such a condition should beregarded
as the correct local formulation of the second
principle
for the materials inquestion.
The
procedure
we shall follow will be that ofrepeating
the classicalreasoning
in a wayappropriate
to theapplication
at which we areaiming.
In
doing
so we shall have toemphasize
themeaning
of the mainconcepts
introduced in classicalthermodynamics.
This is done in Sections 2 and 3 where aprecise
definition of the words state, process,cycle, equilibrium
and
reversibility
isgiven.
Section 4 deals with the mathematical formulation of the secondprinciple
in the classical case ofhomogeneous
processes.The aim is to
point
out the fact that this formulationis fully expressed by
apostulate
relevant tocyclic
processesperformed by systems
at uniform(but,
of course, timedepending) temperature.
In Section5,
theconcept
of reversible entropy will be introduced and the way in which the notion ofentropy
has to be defined in the case ofnon-equilibrium/non-homogeneous
processes will be discussed. This should
provide
an answer to the often raisedquestions
on whetherentropy
can be defined innon-equilibrium situations,
on whether
entropy
is aquantity
which can be measured in non-reversible situations and on whetherentropy
is aquantity
which can beuniquely
defined
(to
within aconstant)
for each material. As a main result Section 5 contains theproof
that the so-called Clausius-Planckinequality
is the correctlocal form of the second
principle
ofthermodynamics.
Theanalysis
shouldmake clear that this
inequality
is valid ingeneral
fornon-equilibrium/
non-homogeneous
processesprovided,
of course, that these processes are not so tumultuous that amacroscopic description
of thephenomenon
becomes
meaningless.
2. THE DEFINITIONS OF
STATE,
PROCESS AND CYCLE
We shall define a material system
(or
moresimply
a system or abody)
as a
portion
of matter whose behaviour we want to describeby
means of aAnnales de 1’Institut Henri Poincaré - Section A
suitable theoretical model.
By
state of thesystem
we shall denote a collec- tion of values assumedby
the set of variables which aresupposed
to besufficient to define the
kinematical-physical-chemical
situation of thesystem.
The
problem
ofselecting
andidentifying
the state variables of asystem
is aproblem
which must be considered whenever we have toapply
thetheory
to a
specific system.
Thisproblem, however,
can bedisregarded
in thepresent general analysis.
From the definition of state it follows that two kinematical-physical-chemical
situations of asystem
are the same whenever all the state variables assume the same values in both the situations.A process is an ordered and continuous succession of states. Time may be assumed as
parameter
of this succession. We cannot assume,however,
that time itself is a state variable if we suppose as we shall do-that asystem
can be in the same state at two different instants.
Let 11 and t2
denote two values of time t. We shall say that a processoccurring between 11 and t2
is acyclic
process(or
acycle)
if the state of thesystem
at t = tl is the same as the state of thesystem
at t =t2.
Time rates of state variables may, of course, be state variables themselves. In apurely
mechanical
theory,
forinstance,
to define the state variables of a materialpoint
we have tospecify
notonly
theposition
of thepoint
but also itsvelocity
and its acceleration : two materialpoints
in the sameposition
butwith different velocities and accelerations are,
clearly,
in different statesaccording
to the above definition of state.Similarly,
when athermodynami-
cal
theory
isconsidered,
the time rates of the absolutetemperature
0 are ingeneral
state variables. To be convinced about this observe for instance that the situation of abody
at uniform buttime-increasing temperature
iscertainly
different from the situation in which thetemperature
of thebody
is constant
(thermal equilibrium)
ortime-decreasing
ortime-increasing
at different rate ; all the other state variables
being kept
constant.The above definitions of state
and, consequently,
ofcycle
areparticu- larly
useful inextending
in anunambiguous
way the results of classicalthermodynamics
to themacroscopic thermodynamics
ofnon-homogeneous
processes. Classical
thermodynamics
deals withequilibrium
processes.For this reason
quantities representing
time rates areautomatically
excludedfrom the set of the variables of a system. It is
concerned,
moreover,mainly
with the case in which the state variables do not vary
throughout
thesystem.
In such a situation it is
possible
todevelop
thetheory
withoutintroducing
state variables which
represent
time rates or which can assume different values in the variousparts
of thesystem (cf.
for instance the classical caseof a gas
undergoing
anequilibrium
process ; in this case the state is definedby
three numbersrepresenting respectively
thevolume,
the pressure and thetemperature
of thesystem).
While this restricted notion of state isperfectly adequate
to the scope of the classicaltheory,
it has to beproperly
widenedif we want to deal with
non-homogeneous and/or non-equilibrium
pro-cesses.
Vol. XXVII, nP 2 - 1977.
210 A. PAGLIETTI
3. REVERSIBLE AND
QUASI-STATIC
PROCESSESIn classical
thermodynamics
the notion ofreversibility
isusually
intro-duced
through
thefollowing
or anequivalent
definition(cf.
e. g.[4], §
112and
[6],
p.12) :
A process is reversible if:
(a)
it can beperformed by
asystem
both accord-ing
to the direct succession of statesdefining
the process(direct process)
and
according
to the inverse succession(inverse process); (b) during
theinverse process not
only
thesystem
but also thesurroundings
recover thesame states
they
assumeduring
the direct process.A
system
is said to be in a stateof equilibrium
when all its state variables whichrepresent
time rates vanish.Accordingly,
an ordered succession of states ofequilibrium
is called anequilibrium (or quasi-static)
process. Itmust be
emphasized
that asystem
can neverundergo
in a finite time intervala
quasi-static
process which is different from the trivial one whichalways keeps
thesystem
at the same state. For asystem
to pass from oneequilibrium
state to another
equilibrium
state some state variables mustchange. Hence,
the time rates of these variables must be different from zero
and, therefore,
the passage from an
equilibrium
state to another one cannot beaccomplished by
aquasi-static
process.From the
previous
definitions we can infer that a reversible process must be aquasi-static
one.Indeed, during
the inverse process the state variablesrepresenting
time rates assumeopposite
values to thosethey
assumeduring
the direct process.
Thus, they
must vanish in order thatduring
the inverse process thesystem
may attain the same states it attainsduring
the directprocess.
Since a
quasi-static
process is not, ingeneral,
a real process, it follows that asystem
cannotundergo
inpractice
a reversible process which is different from a trivial one whichkeeps
thesystem
at the same state. Thata reversible process in a mere theoretical abstraction which does not corres-
pond
to any realizable process waspointed
outeffectively by
Duhem([3],
§ 58). However,
Duhem(loc. cit. )
consideredquasi-static
processes asreversible;
whileaccording
to the definitions hereadopted
aquasi-static
process is not, in
general,
a reversible one. This is better shownby
the follow-ing example.
A bar ofconducting
material iskept
at non-uniformtemperature by putting
its ends in contact with two heat reservoirs at differenttempera-
tures. If the reservoirs are
big enough
asteady-state
situation will be reached in which the bar is in anequilibrium
state since all its state variables repre-senting
time rates vanish. In thissituation, however,
the state variablesvary
along
the bar since o so does. We canregard
the processundergone by
the barduring
a certain time interval in thesteady-state
situation as atrivial
quasi-static
process in which the state of thesystem
does notchange.
Annales de l’Institut Henri Poincare - Section A
In the same
steady-state
situation we canregard
the processundergone by
thesystem during
a successive time interval as the inverse of the above process. The latteris, therefore, trivially
invertible. It is not,however,
reversible because at the end of the inverse process thesurroundings
are ina different situation from that at the
beginning
of the direct processowing
to the transfer of a certain amount of heat from one reservoir to the other.
The above
example
shows that there areequilibrium
states which cannotbelong
to any reversible process. In the considered case this was a conse-quence of the presence of a
stationary temperature gradient.
Ingeneral,
a
given equilibrium
state cannotbelong
to a reversible process if we cannotprevent
thesurroundings
fromundergoing changes
in their stateby keeping
the
system
at theequilibrium
state. To denote a state ofequilibrium
whichcan
belong
to a reversible process we shalladopt
theexpression
stateof
reversible
equilibrium.
4. THE SECOND PRINCIPLE OF THERMODYNAMICS
The second
principle
ofthermodynamics
can beexpressed by
one of thefollowing equivalent postulates :
(A)
In a systemof
bodies atdifferent temperatures
it isimpossible
totransfer
heatfrom
a colder to a hotterbody by
meansof
a process which leaves undiminished the internal energyof
the system and does notrequires
the expense
of
mechanical workby
thesurroundings.
(B) (Impossibility of perpetual
motionsof
the secondkind) .
It isimpossible by
meansof
an inanimate material agency to deriveuseful
mechanical workfrom
anyportion of
matterby cooling
it below thetemperature of
the coldestof
thesurrounding objects.
’Postulate
(A)
is due in essence to Clausius[1]
whilepostulate (B)
wasexpressed by
Kelvin[2].
It is well known that these twopostulates
areequi-
valent. The
proof
issimple
and can be found in many books on thermo-dynamics (see
e. g.[6]
and[7]).
Let
Q
denote the amount of heat absorbedby
abody
in the unit timeand suppose that the
body undergoes
acyclic
process. Let 8 denote the absolutetemperature
of thebody
and suppose thatduring
thecycle
thebody
is at uniformtemperature.
Of course ~ maydepend
on time. A mathe-matical formulation of
postulates (A)
and(B)
is thefollowing :
(C)
For everysystem undergoing
acycle
at uniform(but
ingeneral time-depending)
temperature () the relationVol. XXVII, no 2 - 1977.
212 A. PAGLIETTI
holds
for
reversiblecycles. Whereas, if
acycle
is not reversible the relationmust hold. In no
cycle
can the valueof
the aboveintegral
bepositive.
In the above formulae the
symbol (? means integral along
thecycle,
while the indices rev and irr
emphasize
that thecycle
is reversible or irre-versible, respectively (1).
The
hypothesis
of uniformtemperature
is notonly
an essentialpart
ofpostulate (C)
but is also useful to eliminate anyambiguity
in themeaning
ofthe
quantity
0 in theintegrals (4.1)
and(4.2).
Thishypothesis by
no waymeans that
postulate (C)
does not introduce any restriction insystems
at non-uniformtemperature.
Since(C) applies
to everysystem
at uniformtemperature
it mustapply,
inparticular,
to each infinitesimal(and
thusat uniform
temperature)
element of asystem
at non-uniformtemperature.
However,
the very fact that(C)
refers tosystems
orparts
of them at uniformtemperature
entails that in(4.1)
and(4 . 2)
thequantity
0 must beregarded
as a function of t
only. Any possible dependence
of o on the variablesdescribing
theposition
of thepoints
of thesystem
to which(4 .1 )
and(4 . 2)
are
applied
is excludedby
the fact thatpostulate (C)
is a statement relevantto
portions
of matter at uniformtemperature.
The classical
proof
that(C)
isequivalent
to(A)
or(B) hinges
on thefamous theorem on
efficiency
of heatengines
enunciatedby
Carnot andproved
in a correct wayby
Clausius(2).
We arefollowing, however,
the brillantexposition by
Fast([6],
p.24-36)
which has theadvantage
of esta-blishing (4.1)
and(4.2)
withoutintroducing
the notion ofentropy.
In classical
single-phase
continua thequantity Q
is considered to becomposed
of the contributions of theheating flux
vector h and of thespecific heating supply
s. We shall assume that h is outward directed withrespect
to the surface of the
body
whenever itrepresents
an amount of heat whichflows into the
body
in the unittime,
and that s ispositive
whenever it(1) It may be worthwile to remark that in postulate (C) it is tacitly assumed that Q does
not vanish identically during the cycle. If Q == 0 during the cycle, then (4 .1 ) is satisfied
irrespectively on whether it is applied to a reversible or to an irreversible cycle. It follows
that postulate (C) is a non-trivial statement only when applied to a system (or a part of it) which loses or absorbs heat during the process. This is natural since the second principle is concerned with transformation of heat into work and, therefore, does not impose any restriction to systems undergoing processes in which each element does not absorb or
lose any amount of heat.
(2) The proof given by Caratheodory is free from any reference to heat engines. Its starting point, however, is a postulate of the second law which can be shown to be com-
pletely equivalent to the above (A), (B) or (C) (see [7], chap. 8).
Annales de l’lnstitut Henri Poincaré - Section A
represents
an amount of heat absorbedby
thebody
in the unit time. We can,therefore,
expressQ
aswhere aB is the external surface of the system
B, n
is the outward oriented unit normal to the surface element dA ofaB,
p isthe
massdensity
and dV isa volume element of B.
By applying
thedivergence
theorem weget
from(4 . 3)
When a
system
of infinitesimal volume isconsidered,
we canexploit (4.4)
and express
(4 .1 )
and(4 . 2)
in the formand
respectively.
These relations can be considered as the localequivalent
of
(4 .1 )
and(4 . 2).
5. LOCAL FORM OF THE SECOND PRINCIPLE IN THE CASE OF INFINITESIMAL PROCESSES
Relations
(4.5)
and(4.6)
are relevant tocyclic
processes. Inpractical applications, however,
it is often convenient to express the secondprinciple
in a form which is valid for every infinitesimal process
(3).
This can beachieved
by introducing
the notion ofentropy.
In the case of reversible processes this notion issuggested spontaneously by equation (4 .1 ) :
since(4 .1 )
must be valid for an
arbitrary
reversiblecycle,
a well-known chain ofreasoning
leads to the conclusion that there must be aquantity
H acontinuous and
single-valued
function of the variablesdefining
the statesof reversible
equilibrium with
theproperty
that(3) By an infinitesimal process we understand a process relevant to an infinitesimal variation of t; t being considered as parameter for the states assumed by the system during
a process.
Vol. XXVII, n° 2 - 1977. 14*
214 A. PAGLIETTI
The
quantity
H isusually
calledentropy;
it is definedby (5.1)
to within anarbitrary
constant. We shalladopt
for H the denomination of reversibleentropy
toemphasize
that this function is definedby (5.1)
for states ofreversible
equilibriuin only.
Once thequantity
H isintroduced,
we canobtain from
(4.1)
the relationsHere 1 and 2 denote two states
belonging
to the reversiblecycle
takeninto consideration. These states are,
obviously,
states of reversibleequi-
librium. Since the states 1 and 2 can be in the same infinitesimal
neigh- bourhood,
we deduce from(5.2)~
that for reversible processeswhich is the
equivalent
of(4.1)
for the case of infinitesimal processes.When
considering
a continuousmaterial,
it is convenient to introduce thequantity M
definedby
We shall refer
to 17
as to thespecific
reversibleentropy.
From(4 . 4)
and(5 .4)
we can deduce the local form of
(5 . 3) :
This relation holds for reversible processes because so does
(5.3).
Since forreversible processes
grad 03B8
--_ 0(cf.
end of Section3),
the term div h shouldbe
dropped
from(5.5) whenever
the constitutiveequation for h
is such that h = 0 ifgrad
0 --_ 0. Inparticular,
asPipkin
and Rivlin[5] proved
that
for central symmetric
materials the vector h must vanish if thetempe-
rature
gradient vanishes,
the termcontaining
div A should bedropped
from
(5.5)
when centralsymmetric
materials are considered.Let us now focus our attention on the case of irreversible processes.
Consider an irreversible process which takes the
system
from state 1 tostate 2 and suppose that both 1 and 2 are states of reversible
equilibrium.
Once state 2 is
reached,
let thesystem
bebrought
back to state 1through
a reversible process
(this
process ispossible
since states 1 and 2 are assumedto be states of reversible
equilibrium).
In this way we have constructeda
cycle
which is irreversible because the process from 1 to 2 is irreversible.From
(4 . 2)
and(5 . 2) 3
weget, therefore,
Annales de l’Institut Henri Poincaré - Section A
That is
At this
point
theprocedure usually
followed in classicalthermodynamics
makes
appeal
to the fact that(5 . 7)
must be valid inparticular
when states 1and 2 are in the same infinitesimal
neighbourhood
and the process from 1 to 2 is an infinitesimal one. In this way it is inferred from(5.7)
for irre-versible processes
Such a
procedure
does not seem correct. Sinceby hypothesis
the states 1and 2 which appear in
(5.7)
are states of reversibleequilibrium
and sincean infinitesimal process between two states of reversible
equilibrium
in thesame infinitesimal
neighbourhood
is a reversible one, it follows that for this process relation(5.3)
must be valid andthat, therefore,
the abovelimit
procedure
cannot leadanywhere
but to the same result(5.3).
To arrive at a relation
analogous
to(5. 5)
but valid also for irreversible processes consider twogeneric
states(not necessarily
of reversibleequili- brium),
say I* and2*,
in addition to two states of reversibleequilibrium,
say 1 and 2.
Suppose
that thesystem undergoes
acyclic
processcomposed
of the
following
successivephases :
a process from I* to2*,
a process from 2*to
2,
a reversible process from 2 to 1and, finally,
a process from 1 to I*that
completes
thecycle.
The processes( 1 *, 2*), (2*, 2)
and( 1, 1 *)
are, ingeneral,
non-reversible. Ingeneral, therefore,
thecycle
is irreversible and from(4.1)
and(4.2)
we can deduce thatthe
equality sign holding
when thecycle
is reversible.By applying (5.9)
to an infinitesimal element and
recalling (5.2)3, (5.4)
and(4.4)
we inferthat
where in the last two
integrals
we have forsimplicity kept
the notationQ
for div h + ps.
By introducing
thequantity ~(1,2,1~)
definedby
we can write
(5.10)
in the formVol. XXVII, no 2 - 1977.
216 A. PAGLIETTI
Let y denote the space of the states of reversible
equilibrium
and letn(l *, 2*)
be the set of all the
couples
of processes(1, 1 *)
and(2*, 2)
forassigned
I*and 2*. As the
couple
ofstates {1,2}
varies in J and as thecouple
ofprocesses {(1, 1*), (2*, 2)}
varies inn(l*, 2*),
thequantity ~(1,3,1~,2*)
assumes different values. Let
~(1~2*)
denote the supremum of the values assumedby ~(1,2.1~) for {1,2}~
andfor { (1, 1*), (2*, 2) } 8il(1 *,2*),
that is
is thus
defined
as asingle-valued
function of the states I* and 2*and can assume any real value between - oo and + oo. For
simplicity
weshall assume that
~ 1~2*)
is asmooth function
of the state variablesdefining
1 *and 2*. Since relation
(5.12)
must be met for every choice of states 1 and 2 and for every process(1, 1 *)
and(2*, 2),
it follows thatIn
particular
when the process is an infinitesimal one(see
footnote3)
which takes the
system
from the state I* to the stateI*
in the infinitesimalneighbourhood
of1 *,
we have from(5.14)
thatwhere the
quantity ~
is definedby
the relationWe shall
call 11
thespecific
entropy of the material. Relation(5 . 1 5)
is some-times called Clausius-Planck
inequality,
it has been deduced here as anecessary consequence of
postulate (C).
Since I* and
f*
are not, ingeneral,
states ofequilibrium,
theentropy
above defined is relevant tonon-equilibrium
states. From(5.11)
and(5.13)
we see that the function
~~ 1*,2*~ and, hence,
the function 11 can be deter- minedthrough experimental
measurements of the amount of heat absorbedduring
irreversibleprocesses; ~ being
aquantity
which can beexperimentally
determined
by
standard calorimetricprocedures (cf. [6],
p.83-87).
Thatfor each
system
there must be(to
within aconstant) only
oneentropy
function 11 is a consequence of the factthat 11
is definedthrough
the supre-mum
(5.13).
It is an easy matter to
verify
that for reversible processesto within a constant, and
that, therefore,
theentropy 11
as above defined is a consistentgeneralization
of the reversibleentropy ~. Indeed,
since rela- tion(4.1) implies
that for reversible processes the timeintegral
ofQ/0
Annales de l’Institut Henri Poincaré - Section A
depends only
on the initial and on the final state of the process, it follows from(5.11)
that when I* and 2* are states of reversibleequilibrium
thequantity ~(1,2,1*,2*)
does notdepend
on the states 1 and 2.Consequently,
when reversible processes are considered. From
(5.18),
from(5.16)
andfrom the fact that these relations can be
applied
to any reversible processwhatsoever,
it follows thatThus relation
(5.17)
follows to within an inessential constant.’ ’
Inequality (5.15)
has been deduced as a necessary consequence of the secondprinciple
ofthermodynamics. Conversely, by denying (5.15)
wecan arrive at a contradiction of
postulate (C).
To provethis,
consider asystem undergoing
an infinitesimal process which starts from the state I*and ends to the state I* in the infinitesimal
neighbourhood
of I*.Suppose
that for this process
in contradiction with
(5.15).
For this infinitesimal process wehave, clearly,
that
In view of definition
(5.16)
we can thus write(5.20)
in the formLet 1 and 2 be two states of reversible
equilibrium
and consider thecycle
I* - 1 * - 2 - 1 - 1 *. From
(5.13)
we have that thequantity
relevant to this
cycle
and definedby (5 .11 )
must be such thatBut from
(5 . 23), (5.22)
and from(5.11)
it follows thatwhich contradicts
(4. 5)
and(4.6) and, hence, postulate (C).
Relation(5.15)
represents,
therefore,
a mathematical formulation of the secondprinciple,
which is
equivalent
to formulation(C)
for the case of classicalsingle-phase
continua. To assume any other not
equivalent
form would be the same as Vol. XXVII, n° 2 - 1977.218 A. PAGLIETTI
to
admitting
thepossibility
ofperpetual
motions of the second kind(cf.
cri-ticism in
[8]).
Observe, finally,
that theentropy
definedby (5.6)
is a state functiondepending
on the materialmaking
up thesystem.
Itis, therefore,
a consti- tutivequantity
that has to be determinedby appropriate experiments.
Accordingly,
there are no apriori
restrictions to the form which theentropy
function can assume,provided,
of course, that this form fulfils thegeneral requirements
of a correctphysical description (cf.
e. g., therequirements imposed by
theprinciple
of materialframe-indifference).
In someapproaches
to
non-equilibrium thermodynamics,
theentropy
of the material isexpressed
as the sum of
products
ofappropriate forces and fluxes.
Whether or not suchan
expression
for theentropy
function can be achieved in anunambiguous
way for every
material,
is aproblem
still debated. Thisproblem, however,
is outside of the scope of thepresent
paper, whose aim has been that ofestablishing
a correct local formulation for the secondprinciple
of thermo-dynamics, quite independently
of anyparticular
form of the relation express-ing
theentropy
as a function of the state variables of thesystem.
Since the secondprinciple
deals with everypossible thermodynamic system,
there is noreason to exclude any
particular
form for theentropy
function.It is
perhaps
worthwhile to stress, moreover, that theapproach consistently adopted throughout
this paper is themacroscopic
one. Of course, this isnot the
only approach by
which the behaviour of a realsystem
can be des- cribed. A monoatomic gas, forinstance,
can be described eitherby regarding
it as a continuous
material,
orby considering
it ascomposed
of a collectionof small hard
spheres
in random motion(kinetic theory) .
In the first case,we
assign
the constitutiveequations
for energy,entropy,
stress and heat flux vector. In the second case, we introduceparticular hypotheses
for theforces the
spheres
exert on each other and for the statistical distribution of thespeed
of thespheres.
Both the models may lead to consistent results whenthey
areapplied
to describe the behaviour of the gas in a certain range of processes.Since, however, they originate
from different idealizations of the realsystem, they
may lead todiscrepant
results whenapplied
to thestudy
of processes for which the above idealizations prove to be not
equivalent.
It is not
surprising, therefore,
that a constitutivequantity,
say theentropy,
determined
experimentally by considering
a monoatomic gas as acontinuum,
does notgenerally
coincide with theanalogous quantity
calculatedthrough
the kinetic
theory.
This does not mean that the real gas possesses two diffe- rententropies,
butmerely
means that the two mathematical models associated with it are different.ACKNOWLEDGMENT
This work was done at the Mathematical Institute of the Oxford Univer-
sity during
the tenure of a N. A. T. O.Fellowship
from the Istituto di Scienza delleCostruzioni, University
ofCagliari, Italy.
Annales de l’Institut Henri Poincaré - Section A
REFERENCES
[1]
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[3] P. DUHEM, Thermodynamics and Chemistry, 1st ed., English transl. by G. K. BURGESS, Wiley, London, 1903.
[4] M. PLANCK, Treatise on Thermodynamics, 3rd ed., English transl. from 7th German ed.
by A. OGG, Longmans-Green, London, 1927.
[5] A. C. PIPKIN and R. S. RIVLIN, The formulation of constitutive equations in conti-
nuum physics. Tech. Rap. DA 4531/4 to the Dept. of the Army, Ordnance Corps,
1958.
[6] J. D. FAST, Entropy, 2nd ed., MacMillan, London, 1970.
[7] M. W. ZEMANSKY, Heat and Thermodynamics, 5th ed., McGraw-Hill, Tokyo, 1968.
[8] A. PAGLIETTI, On a local form of the second principle of thermodynamics (to appear).
(Manuscrit revise, reçu le 26 janvier 1977).
Vol. XXVII, n° 2 - 1977.