WEBVTT

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GIAN PAOLO BERETTA:
Good afternoon.

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So here we are.

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And let's see where we are.

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We have introduced this
energy versus entropy diagram

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to summarize concepts.

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And we have obtained these
important inequalities

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that I called generically
Clausius inequalities that

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essentially talk about--

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say something about
how much entropy

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must be exchanged
between two systems

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if these two systems start
in stable equilibrium states

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and they need to exchange
energy with no other effects.

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So if this is the curve
for the stable equilibrium

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states for system A and
this is for system B,

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we suppose that the system
A starts in this state

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and that we want to extract
this much energy from it

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and give it to system
B. We realize that there

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is no way to-- since
there are no states

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below the initial state, we need
to extract also some entropy.

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But the problem
is that system B--

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so if we extract
entropy from system A,

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that entropy can
only go into system B

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because there are no
other external effects.

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But starting from
this state, system B,

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and receiving this much
energy, the amount of entropy

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that it can accommodate
is only this much,

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which is called S max.

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So that's the maximum amount of
entropy that B can accommodate.

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Whereas for system A, this is
the minimum amount of entropy

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that it needs to
give to system B

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in order to find a state
with this lower energy level.

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So we are left with a
possibility of possible states

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that are on these dashed
lines for system A

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and for system B that
correspond to entropy transfers

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within the range allowed
by these constraints

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that we have described.

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So that turns out to be
writeable as a couple

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of inequalities.

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The Clausius
traditional statement

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is, as we have seen it,
for infinitesimal amounts

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of energy transfers.

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This is for finite.

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But the concept is the same.

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So today, I wanted to talk
about some traditional results.

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And we still need to define
what we mean by heat.

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First of all, we define
what we mean by work.

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So work is a mode of
interaction in which

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there is no entropy transfer
and no transfer of amounts

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of constituents.

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So that's, for example, what
happens in a weight process.

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In a weight process, if
during the entire process,

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there are no external effects,
then the weight process

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experiences--

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the system experiences
a work interaction.

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As you may read here, it
says that the weight process

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may be adiabatic.

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We call adiabatic a
process in which there

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are only work interactions.

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And then we say, well, a weight
process may be adiabatic.

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Why maybe and not is adiabatic?

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Well, because a weight
process is a process

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in which the only
net external effect

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is the lifting or lowering
of a weight, the net effect.

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But you could have
some temporary effects

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that are initially
done and then undone,

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which may not be describable by
lifting or lowering a weight.

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So in that case, it's
still a weight process.

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But during the process,
there were interactions

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that may not be work.

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But for simplicity, if
you want to fix ideas,

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a good example of
an adiabatic process

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is a weight process in which
there are no entropy transfers

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all along the process.

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Anything that has an entropy
transfer, we call it non-work.

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So non-work is a very
broad class of processes,

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of types of interaction.

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And in this broad class, there
is one limiting condition

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that we call heat interaction.

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So we will see in a moment
what is the defining

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idea behind what we call heat.

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It is a limiting process.

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And it doesn't exhaust all the
possible non-work interactions.

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So not all non-work
interactions are heat.

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And in fact, I already
anticipated the last time

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that, during a heat
interaction, we

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have a very well-defined
ratio between the energy that

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is exchanged, that we call
heat, and the entropy that

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is exchanged.

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And the ratio is equal--

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energy over entropy
is the temperature

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at which that interaction
occurs, so much that therefore,

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in order to characterize
a heat interaction,

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we only need to say it's heat,
how much energy is transferred,

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and what is the temperature
at which it is transferred.

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But what's the defining
criterion for heat?

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One way to put it is, we want
to define an interaction, which

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is completely
distinguishable from work,

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so an interaction
in which these two

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systems, say system A and system
B, exchange energy and entropy.

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And nothing, no
fraction of the energy

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that is exchanged between the
two, can be recognized as work.

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What does it mean?

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All right, we do
it operationally.

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Let's say that we extract
some energy from system A.

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And let's suppose that
we intercept that energy.

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And before giving
it to B, we feed it

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to some machinery,
some machinery that

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will try, at its best, to split
that energy into a part that

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is recognizable as
work and the rest.

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Sometimes, I mean,
traditionally you

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would call it a Carnot engine.

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But let's call it
a cyclic machinery,

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cyclic because it has to
return to its initial state.

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And so whatever
it does, it's not

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because you consume the machine,
but because of the operations

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of the machine.

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OK.

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So in this situation, suppose
we extract this much energy

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and this much entropy.

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We feed it to the
engine, to the machinery.

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How much work can we extract?

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Well, this is a standard
problem in thermodynamics

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that gets solved by writing
energy and entropy balances.

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So we write energy and entropy
balances for system A and system

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B. We also assume that system
A and system B begin and end

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in stable equilibrium states.

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And we write this
bunch of equations.

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If you count the equal signs,
it's how many equations?

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1, 2, 3, 4, 5, 6,
7, 8 equations.

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Considering the
initial temperatures

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as fixed parameters,
the variables here

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are the various
entropy exchanged

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and the energy and entropy
changes for system A and system

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B. If you count them, I think
there are nine variables, eight

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equations.

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You cannot solve the system.

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But you can solve it for a
ratio of two of those variables.

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And we choose the ratio
that we are interested in,

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namely the work that
has been separated out

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of that stream over
the inlet energy, inlet

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into the cyclic engine.

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So this ratio, as we
all, because we've all

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taken thermodynamics
before, it's

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the Carnot ratio between
the two initial temperatures

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of these systems.

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So this says that if these two
temperatures are different,

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this ratio is not 0.

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It's a definite number.

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Suppose the system B is at
300K and system A is at 600K.

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This is 300 over 600.

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That Is 1/2.

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So 1 minus 1/2 is 50%.

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So that means that
the cyclic engine here

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could split 50% of the
received energy from A

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and make it go into
the work channel.

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Sure.

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If we want to complete the job
once, we have split this energy

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and give it to the weight,
then we take the weight back

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and give that
energy to system B.

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So the end result is the same.

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We transfer the energy from A
to B with no external effects.

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But in between, we
manage to recognize

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a part of what flows from one
system to the other as work.

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That's not what we
want to call heat.

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We will call heat
only in the limit

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in which this ratio goes to 0.

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And that goes to 0
only in the limit

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in which the two temperatures
get equal or very close

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to one another.

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And in terms of that train of
inequalities that we have seen,

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the Clausius
inequality last time,

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that interval of values, if
the two temperatures are equal,

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shrinks to a single value.

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And therefore, we get a
definite entropy transfer

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for a given energy transfer.

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And that's how we get
the famous equation

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that delta S, the
entropy exchanged,

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is the energy exchanged
over T, so Q over T.

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And of course, I have
stressed it so many times.

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But we noticed that we have
defining heat here using

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entropy.

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Usually, it's the
other way around.

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The traditional
expositions start

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from some hand-waving
definition of heat,

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and then some definition
of temperature.

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And then Q over T
becomes the entropy.

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And that's the--

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I call it the hand-waving
heuristic definition of entropy

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that, to be frank
with you, is what

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got me started with this
subject because I was so unhappy

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of the way I was
explained the subject

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that I wanted to study it more.

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It's funny.

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You hate the subject because
you don't understand it.

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And then you become
to love it because you

00:14:17.360 --> 00:14:18.720 align:middle line:90%
want to understand it.

00:14:18.720 --> 00:14:21.260 align:middle line:90%


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All right.

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But how does this
definition match

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with our usual understanding?

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Because if I ask you
what's heat, well,

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heat is the energy
that is transferred

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between systems at different
temperature, you would say.

00:14:39.860 --> 00:14:42.770 align:middle line:84%
Well, we just said,
no, heat is the energy

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that's transferred between
systems at the same temperature.

00:14:48.570 --> 00:14:52.440 align:middle line:90%
So is there something wrong?

00:14:52.440 --> 00:14:54.120 align:middle line:90%
In fact, there isn't.

00:14:54.120 --> 00:14:57.240 align:middle line:84%
Because, think of
the typical model

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that we adopt in heat transfer.

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Suppose we have two systems
at different temperatures.

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And we put them in contact.

00:15:07.260 --> 00:15:18.920 align:middle line:84%
In the region of contact,
their initial equilibrium,

00:15:18.920 --> 00:15:20.980 align:middle line:84%
if they had a
temperature initially,

00:15:20.980 --> 00:15:24.230 align:middle line:84%
as soon as they get in contact,
in the region of contact,

00:15:24.230 --> 00:15:27.010 align:middle line:84%
you get a non-equilibrium
situation.

00:15:27.010 --> 00:15:38.930 align:middle line:84%
But we may describe this system
as a composite of many smaller

00:15:38.930 --> 00:15:40.672 align:middle line:90%
systems.

00:15:40.672 --> 00:15:42.830 align:middle line:84%
In fluid mechanics,
you would call them

00:15:42.830 --> 00:15:44.705 align:middle line:90%
infinitesimal fluid elements.

00:15:44.705 --> 00:15:47.470 align:middle line:90%


00:15:47.470 --> 00:15:50.210 align:middle line:84%
In a two-dimensional
problem, you

00:15:50.210 --> 00:15:58.550 align:middle line:84%
could have infinitesimal
slices of your solid or body.

00:15:58.550 --> 00:16:01.280 align:middle line:90%
And then you may assume that--

00:16:01.280 --> 00:16:04.740 align:middle line:84%
we will return, when
we do non-equilibrium,

00:16:04.740 --> 00:16:07.040 align:middle line:84%
we return very
much to this idea--

00:16:07.040 --> 00:16:13.670 align:middle line:84%
we subdivide our
system in such a way

00:16:13.670 --> 00:16:19.880 align:middle line:84%
that each local
subsystem is still

00:16:19.880 --> 00:16:23.570 align:middle line:90%
in a non-equilibrium state.

00:16:23.570 --> 00:16:26.570 align:middle line:84%
But it is not too
far from equilibrium.

00:16:26.570 --> 00:16:30.090 align:middle line:84%
So it turns out
that we can assume

00:16:30.090 --> 00:16:37.990 align:middle line:84%
that this is what we do when
we describe a temperature

00:16:37.990 --> 00:16:42.577 align:middle line:90%
distribution in our solid.

00:16:42.577 --> 00:16:44.410 align:middle line:84%
Temperature distribution
means that there is

00:16:44.410 --> 00:16:46.220 align:middle line:90%
a temperature at each location.

00:16:46.220 --> 00:16:50.380 align:middle line:84%
So that means that each
infinitesimal element

00:16:50.380 --> 00:16:53.080 align:middle line:84%
is close enough to a
stable equilibrium state

00:16:53.080 --> 00:16:54.670 align:middle line:84%
that you can assign
the temperature

00:16:54.670 --> 00:16:56.085 align:middle line:84%
of that stable
equilibrium state.

00:16:56.085 --> 00:17:02.106 align:middle line:90%


00:17:02.106 --> 00:17:05.250 align:middle line:84%
And the fact that the
temperature distribution

00:17:05.250 --> 00:17:12.390 align:middle line:84%
is typically, except
extreme cases, continuous

00:17:12.390 --> 00:17:16.890 align:middle line:84%
means that if you look at it
from the small partitioning

00:17:16.890 --> 00:17:22.050 align:middle line:84%
point of view, each element
has a temperature, which

00:17:22.050 --> 00:17:27.359 align:middle line:84%
differs only slightly from the
adjacent element, and so on,

00:17:27.359 --> 00:17:29.010 align:middle line:90%
by continuity.

00:17:29.010 --> 00:17:34.500 align:middle line:84%
So each lamina, or each
element, is at a temperature

00:17:34.500 --> 00:17:40.800 align:middle line:84%
very close to the temperature
of the near, of the neighbor.

00:17:40.800 --> 00:17:43.710 align:middle line:84%
And therefore, the
interaction between them

00:17:43.710 --> 00:17:46.320 align:middle line:84%
is an interaction in
which there is exchange

00:17:46.320 --> 00:17:51.690 align:middle line:84%
of energy and entropy and in
which the two adjacent elements

00:17:51.690 --> 00:17:54.810 align:middle line:84%
have almost the
same temperature,

00:17:54.810 --> 00:17:58.150 align:middle line:84%
which fulfills our definition
of a heat interaction.

00:17:58.150 --> 00:18:00.780 align:middle line:84%
So locally, it is
a heat interaction

00:18:00.780 --> 00:18:02.820 align:middle line:90%
at the local temperature.

00:18:02.820 --> 00:18:04.560 align:middle line:84%
And then with the
other element, it's

00:18:04.560 --> 00:18:08.220 align:middle line:84%
another interaction at a
lower temperature or a higher

00:18:08.220 --> 00:18:09.430 align:middle line:90%
temperature and so on.

00:18:09.430 --> 00:18:12.776 align:middle line:90%


00:18:12.776 --> 00:18:20.800 align:middle line:84%
This describes what I just
said for, say, a solid.

00:18:20.800 --> 00:18:23.410 align:middle line:90%


00:18:23.410 --> 00:18:28.830 align:middle line:84%
So suppose we concentrate on
these infinitesimal elements

00:18:28.830 --> 00:18:34.940 align:middle line:84%
of solid or continuum in
which the coordinate is only,

00:18:34.940 --> 00:18:38.740 align:middle line:84%
let's say, one dimensional,
coordinate is between x and x

00:18:38.740 --> 00:18:39.520 align:middle line:90%
plus dx.

00:18:39.520 --> 00:18:43.030 align:middle line:90%
So it's infinitesimally thin.

00:18:43.030 --> 00:18:47.380 align:middle line:84%
And it is in contact with
the element to the left

00:18:47.380 --> 00:18:49.900 align:middle line:90%
and the element to the right.

00:18:49.900 --> 00:18:56.020 align:middle line:84%
And for simplicity, let's just
study the steady state situation

00:18:56.020 --> 00:19:00.405 align:middle line:84%
here and make the energy
balance and the entropy balance.

00:19:00.405 --> 00:19:03.290 align:middle line:90%


00:19:03.290 --> 00:19:09.350 align:middle line:84%
So if I make the energy
balance to this lamina,

00:19:09.350 --> 00:19:11.570 align:middle line:84%
I should put on
the left hand-side

00:19:11.570 --> 00:19:16.850 align:middle line:84%
the rate of change of
the energy of the lamina

00:19:16.850 --> 00:19:21.050 align:middle line:84%
and, on the right hand
side, the net contributions

00:19:21.050 --> 00:19:23.910 align:middle line:84%
of the interactions to which
that lamina is subjected.

00:19:23.910 --> 00:19:29.360 align:middle line:90%
So it receives Q dot.

00:19:29.360 --> 00:19:31.770 align:middle line:84%
Now, I'm assuming it
is a heat interaction.

00:19:31.770 --> 00:19:35.060 align:middle line:84%
So it receives Q
dot from the left.

00:19:35.060 --> 00:19:38.630 align:middle line:90%
And it gives Q dot to the right.

00:19:38.630 --> 00:19:43.130 align:middle line:84%
If what comes into the left
and goes out to the right

00:19:43.130 --> 00:19:49.390 align:middle line:84%
is balanced, same rates,
the energy balance

00:19:49.390 --> 00:19:53.740 align:middle line:84%
says that the rate of change
or the rate of accumulation

00:19:53.740 --> 00:19:55.650 align:middle line:90%
of energy of my system is 0.

00:19:55.650 --> 00:19:58.845 align:middle line:84%
So that property doesn't
change with time.

00:19:58.845 --> 00:20:02.440 align:middle line:90%


00:20:02.440 --> 00:20:09.040 align:middle line:84%
For entropy, the entropy balance
should be written this way.

00:20:09.040 --> 00:20:12.680 align:middle line:84%
Left-hand side, the rate
of change of the property,

00:20:12.680 --> 00:20:15.730 align:middle line:84%
so the rate of change
of the entropy of--

00:20:15.730 --> 00:20:19.090 align:middle line:90%


00:20:19.090 --> 00:20:22.930 align:middle line:90%
this is our system, the lamina.

00:20:22.930 --> 00:20:24.830 align:middle line:84%
On the right-hand
side, I have two terms.

00:20:24.830 --> 00:20:30.910 align:middle line:84%
The terms having to do with
the net entropy received

00:20:30.910 --> 00:20:33.880 align:middle line:84%
by interaction and
the last term is

00:20:33.880 --> 00:20:37.540 align:middle line:84%
the entropy produced
by irreversibility

00:20:37.540 --> 00:20:38.715 align:middle line:90%
within the system.

00:20:38.715 --> 00:20:43.010 align:middle line:90%


00:20:43.010 --> 00:20:48.730 align:middle line:84%
So from the left, the
entropy that is received,

00:20:48.730 --> 00:20:52.530 align:middle line:84%
the rate with which entropy
is received is Q dot over T.

00:20:52.530 --> 00:20:57.414 align:middle line:84%
And T here is Tx,
T of location x.

00:20:57.414 --> 00:21:00.640 align:middle line:84%
From the right
there is an outflow

00:21:00.640 --> 00:21:05.170 align:middle line:84%
of entropy, which is Q over
T. But here, the temperature

00:21:05.170 --> 00:21:05.780 align:middle line:90%
is different.

00:21:05.780 --> 00:21:07.150 align:middle line:90%
It's T at x plus dx--

00:21:07.150 --> 00:21:10.300 align:middle line:90%


00:21:10.300 --> 00:21:13.330 align:middle line:84%
one with a plus because it's
entering, one with the minus

00:21:13.330 --> 00:21:15.460 align:middle line:90%
because it's leaving.

00:21:15.460 --> 00:21:17.180 align:middle line:90%
And that's the entropy balance.

00:21:17.180 --> 00:21:21.580 align:middle line:84%
So if we assume a steady
state, steady state

00:21:21.580 --> 00:21:25.720 align:middle line:84%
means the state doesn't
change with time.

00:21:25.720 --> 00:21:27.080 align:middle line:90%
The state is what?

00:21:27.080 --> 00:21:28.480 align:middle line:90%
It's the properties.

00:21:28.480 --> 00:21:31.270 align:middle line:84%
So none of the
properties changes

00:21:31.270 --> 00:21:32.810 align:middle line:90%
with time, including entropy.

00:21:32.810 --> 00:21:37.660 align:middle line:84%
So steady state implies
that dS/dt is equal to 0.

00:21:37.660 --> 00:21:45.010 align:middle line:84%
Then using this expression,
we can compute the entropy

00:21:45.010 --> 00:21:47.510 align:middle line:90%
produced by irreversibility.

00:21:47.510 --> 00:21:50.390 align:middle line:90%


00:21:50.390 --> 00:22:00.040 align:middle line:84%
And we recognize here
Tx and Tx plus dx.

00:22:00.040 --> 00:22:02.960 align:middle line:84%
If I divide that by dx,
that's an incremental ratio.

00:22:02.960 --> 00:22:06.975 align:middle line:84%
So that's the derivative
of T with respect to x.

00:22:06.975 --> 00:22:10.940 align:middle line:90%


00:22:10.940 --> 00:22:16.350 align:middle line:84%
T squared at the denominator--
so this is the result.

00:22:16.350 --> 00:22:18.980 align:middle line:84%
It says that the entropy
produced by irreversibility is

00:22:18.980 --> 00:22:24.290 align:middle line:84%
proportional to the heat that
goes through divided by T

00:22:24.290 --> 00:22:27.420 align:middle line:90%
squared and multiplied by the--

00:22:27.420 --> 00:22:33.440 align:middle line:84%
dT/dx is the gradient in
temperature in the x direction

00:22:33.440 --> 00:22:37.120 align:middle line:90%
with the minus sign in front.

00:22:37.120 --> 00:22:39.520 align:middle line:90%
So this tells us a few things.

00:22:39.520 --> 00:22:45.630 align:middle line:84%
First of all, it
tells us in which

00:22:45.630 --> 00:22:52.410 align:middle line:84%
direction Q can exist for a
given temperature distribution

00:22:52.410 --> 00:22:55.800 align:middle line:84%
because the entropy
produced by irreversibility

00:22:55.800 --> 00:23:02.700 align:middle line:84%
can only be positive or 0 if
we were in a reversible case.

00:23:02.700 --> 00:23:05.670 align:middle line:90%
But it cannot be negative.

00:23:05.670 --> 00:23:08.110 align:middle line:90%
So it means that Q dot--

00:23:08.110 --> 00:23:09.600 align:middle line:90%
here, I have a T squared.

00:23:09.600 --> 00:23:14.310 align:middle line:84%
So it means that Q dot
must have opposite sign

00:23:14.310 --> 00:23:16.090 align:middle line:90%
of the gradient in temperature.

00:23:16.090 --> 00:23:19.770 align:middle line:84%
So the Q dot flows
in the direction

00:23:19.770 --> 00:23:24.640 align:middle line:84%
of decreasing temperature,
which is, of course, what

00:23:24.640 --> 00:23:31.875 align:middle line:84%
we knew, what Clausius told us
in another way the other day.

00:23:31.875 --> 00:23:36.050 align:middle line:90%


00:23:36.050 --> 00:23:38.960 align:middle line:90%
The point, though, is that--

00:23:38.960 --> 00:23:42.740 align:middle line:84%
let's look at what
kind of model we're

00:23:42.740 --> 00:23:45.280 align:middle line:84%
doing by assigning
a temperature here.

00:23:45.280 --> 00:23:48.380 align:middle line:90%


00:23:48.380 --> 00:23:51.680 align:middle line:84%
It's really an approximation
that we are making.

00:23:51.680 --> 00:23:56.340 align:middle line:84%
So in the whole of heat
transfer and fluid mechanics,

00:23:56.340 --> 00:24:00.740 align:middle line:84%
when we make the local
equilibrium assumption,

00:24:00.740 --> 00:24:09.100 align:middle line:84%
it is an approximation,
which is good in order

00:24:09.100 --> 00:24:12.880 align:middle line:84%
to assign local properties like
temperature, pressure, chemical

00:24:12.880 --> 00:24:16.770 align:middle line:84%
potentials to the
fluid elements.

00:24:16.770 --> 00:24:20.400 align:middle line:84%
But we should not
take it too literally

00:24:20.400 --> 00:24:27.930 align:middle line:84%
because, if we were truly
in an equilibrium state,

00:24:27.930 --> 00:24:30.220 align:middle line:90%
these things couldn't happen.

00:24:30.220 --> 00:24:33.150 align:middle line:90%
And look at it this way.

00:24:33.150 --> 00:24:37.530 align:middle line:84%
Let's say that this is the E
versus S diagram of my system

00:24:37.530 --> 00:24:39.755 align:middle line:84%
here, the lamina, the
infinitesimal element.

00:24:39.755 --> 00:24:43.380 align:middle line:90%


00:24:43.380 --> 00:24:48.570 align:middle line:84%
Now, yeah, I think I
have it bigger here.

00:24:48.570 --> 00:24:56.240 align:middle line:90%
Now, so the state--

00:24:56.240 --> 00:24:59.930 align:middle line:84%
I draw the state
of this lamina just

00:24:59.930 --> 00:25:03.200 align:middle line:84%
a bit off the stable
equilibrium state curve.

00:25:03.200 --> 00:25:06.070 align:middle line:90%


00:25:06.070 --> 00:25:08.690 align:middle line:84%
And let's see what
happens there.

00:25:08.690 --> 00:25:09.810 align:middle line:90%
So this is the state.

00:25:09.810 --> 00:25:12.580 align:middle line:90%


00:25:12.580 --> 00:25:19.140 align:middle line:84%
The lamina receives both energy
and entropy from the left.

00:25:19.140 --> 00:25:22.050 align:middle line:84%
So that energy and
entropy from the left

00:25:22.050 --> 00:25:24.065 align:middle line:90%
that received from this side--

00:25:24.065 --> 00:25:28.238 align:middle line:90%


00:25:28.238 --> 00:25:30.280 align:middle line:84%
so the left-hand stuff--
from the left-hand side,

00:25:30.280 --> 00:25:35.190 align:middle line:84%
there is a pull that tries
to pull the state up,

00:25:35.190 --> 00:25:37.800 align:middle line:84%
because it wants
to receive energy,

00:25:37.800 --> 00:25:42.870 align:middle line:84%
and to the right, because it
receives an entropy given by Q

00:25:42.870 --> 00:25:50.280 align:middle line:84%
dot over T. The net result
is that the state is

00:25:50.280 --> 00:25:51.970 align:middle line:90%
pulled in this direction.

00:25:51.970 --> 00:25:53.105 align:middle line:90%
It wants to move there.

00:25:53.105 --> 00:25:56.930 align:middle line:90%


00:25:56.930 --> 00:26:01.350 align:middle line:84%
On the other hand, there is also
an interaction to the left--

00:26:01.350 --> 00:26:05.360 align:middle line:84%
I'm sorry, to the right,
which takes things away.

00:26:05.360 --> 00:26:08.660 align:middle line:90%
It takes energy down.

00:26:08.660 --> 00:26:11.990 align:middle line:84%
So it pulls down
the same amount.

00:26:11.990 --> 00:26:13.310 align:middle line:90%
So these are balanced.

00:26:13.310 --> 00:26:18.770 align:middle line:84%
And therefore, the state
will remain at this level.

00:26:18.770 --> 00:26:27.200 align:middle line:84%
But it pulls to the
left a different value

00:26:27.200 --> 00:26:31.820 align:middle line:84%
because the temperature
is different.

00:26:31.820 --> 00:26:35.840 align:middle line:84%
And here, at x plus
dx, the temperature,

00:26:35.840 --> 00:26:43.280 align:middle line:84%
I assume it's smaller, so this
ratio, since it's a denominator.

00:26:43.280 --> 00:26:46.650 align:middle line:84%
The smaller at the
denominator means bigger.

00:26:46.650 --> 00:26:53.540 align:middle line:84%
So it means that this pull to
the left is higher than the pull

00:26:53.540 --> 00:26:54.340 align:middle line:90%
to the right.

00:26:54.340 --> 00:26:57.830 align:middle line:90%
So there is an unbalance.

00:26:57.830 --> 00:27:03.440 align:middle line:84%
And if there weren't entropy
produced by irreversibility,

00:27:03.440 --> 00:27:08.180 align:middle line:84%
this state would follow the
unbalance and go backwards.

00:27:08.180 --> 00:27:17.840 align:middle line:84%
So that is to say that I need
this irreversibility to be

00:27:17.840 --> 00:27:20.930 align:middle line:84%
produced locally in order
to maintain the steady state

00:27:20.930 --> 00:27:22.495 align:middle line:90%
of that fluid element.

00:27:22.495 --> 00:27:25.400 align:middle line:90%


00:27:25.400 --> 00:27:29.100 align:middle line:84%
But in order to produce
entropy by irreversibility,

00:27:29.100 --> 00:27:32.750 align:middle line:84%
I must not be at
stable equilibrium

00:27:32.750 --> 00:27:35.300 align:middle line:84%
because, at stable equilibrium,
the system is happy.

00:27:35.300 --> 00:27:41.300 align:middle line:84%
And it doesn't rearrange
things in order-- it already

00:27:41.300 --> 00:27:42.870 align:middle line:90%
is in the maximum entropy.

00:27:42.870 --> 00:27:47.600 align:middle line:84%
There is no tendency
to produce more.

00:27:47.600 --> 00:27:54.530 align:middle line:84%
So this is to say that there
is a bit of a contradiction,

00:27:54.530 --> 00:27:58.040 align:middle line:84%
or at least that we have to be
careful in understanding what

00:27:58.040 --> 00:28:00.140 align:middle line:90%
the actual assumptions are.

00:28:00.140 --> 00:28:03.120 align:middle line:84%
This state is a
non-equilibrium state.

00:28:03.120 --> 00:28:06.360 align:middle line:84%
Otherwise, it couldn't produce
entropy by irreversibility.

00:28:06.360 --> 00:28:09.420 align:middle line:84%
But it is close to a
stable equilibrium state.

00:28:09.420 --> 00:28:16.100 align:middle line:84%
And therefore, we can use
the idea of temperature

00:28:16.100 --> 00:28:18.280 align:middle line:84%
and assign it to
the fluid element.

00:28:18.280 --> 00:28:20.960 align:middle line:84%
But indeed, what it is
is the temperature that

00:28:20.960 --> 00:28:23.330 align:middle line:84%
would be reached if I
took that fluid element

00:28:23.330 --> 00:28:26.330 align:middle line:84%
and isolate it from
the rest and let

00:28:26.330 --> 00:28:32.600 align:middle line:84%
it relax to equilibrium because
if I shut the interactions left

00:28:32.600 --> 00:28:35.270 align:middle line:84%
and right, this
non-equilibrium state

00:28:35.270 --> 00:28:40.940 align:middle line:84%
will spontaneously move
to stable equilibrium.

00:28:40.940 --> 00:28:45.290 align:middle line:84%
And then it will
have a temperature.

00:28:45.290 --> 00:28:47.600 align:middle line:84%
And that's the
temperature that we assign

00:28:47.600 --> 00:28:49.200 align:middle line:90%
to this non-equilibrium state.

00:28:49.200 --> 00:28:52.700 align:middle line:90%


00:28:52.700 --> 00:28:57.770 align:middle line:84%
This is interesting because
it is the local equilibrium

00:28:57.770 --> 00:29:04.200 align:middle line:84%
model that we are used to
using in fluid mechanics.

00:29:04.200 --> 00:29:08.990 align:middle line:90%
But you can improve.

00:29:08.990 --> 00:29:14.180 align:middle line:84%
And people are doing extensions
of fluid mechanics treatment

00:29:14.180 --> 00:29:20.420 align:middle line:84%
in which you deal with this
little difference in entropy

00:29:20.420 --> 00:29:24.540 align:middle line:84%
because maybe you can
assign a temperature,

00:29:24.540 --> 00:29:26.840 align:middle line:84%
but the entropy of
this state is slightly

00:29:26.840 --> 00:29:32.210 align:middle line:84%
less than the entropy of
a truly equilibrium state

00:29:32.210 --> 00:29:33.390 align:middle line:90%
at that temperature.

00:29:33.390 --> 00:29:40.730 align:middle line:84%
And that difference in
entropy does sometimes--

00:29:40.730 --> 00:29:48.990 align:middle line:84%
has an importance for
certain applications.

00:29:48.990 --> 00:29:51.790 align:middle line:90%


00:29:51.790 --> 00:29:52.290 align:middle line:90%
OK.

00:29:52.290 --> 00:29:57.730 align:middle line:90%


00:29:57.730 --> 00:30:05.670 align:middle line:84%
So now I want to talk about
these very traditional ideas

00:30:05.670 --> 00:30:10.530 align:middle line:84%
of heat engines, heat pumps,
and refrigeration units,

00:30:10.530 --> 00:30:12.850 align:middle line:84%
and see the energy and
entropy that flows.

00:30:12.850 --> 00:30:17.220 align:middle line:84%
And also, it gives
us the opportunity

00:30:17.220 --> 00:30:20.940 align:middle line:84%
to define what we mean by
first and second law efficiency

00:30:20.940 --> 00:30:22.450 align:middle line:90%
of devices like these.

00:30:22.450 --> 00:30:28.120 align:middle line:90%


00:30:28.120 --> 00:30:34.040 align:middle line:84%
So let's start from
what we are seeing.

00:30:34.040 --> 00:30:38.590 align:middle line:90%
So let's do it our own way.

00:30:38.590 --> 00:30:43.180 align:middle line:84%
Suppose we take the
Clausius inequalities

00:30:43.180 --> 00:30:46.690 align:middle line:84%
that we have seen the
other day and remember

00:30:46.690 --> 00:30:56.770 align:middle line:84%
that these subscripts over
the extreme inequalities

00:30:56.770 --> 00:31:00.010 align:middle line:84%
indicate what the
condition should

00:31:00.010 --> 00:31:03.830 align:middle line:84%
be for the strict
equality to hold.

00:31:03.830 --> 00:31:11.260 align:middle line:84%
And here, if you remember,
we have a strict equality

00:31:11.260 --> 00:31:17.200 align:middle line:84%
if the system is in a
stable equilibrium state--

00:31:17.200 --> 00:31:19.210 align:middle line:84%
ends in a stable
equilibrium state and it

00:31:19.210 --> 00:31:24.280 align:middle line:84%
is a reservoir, so that the
second derivative is equal to 0.

00:31:24.280 --> 00:31:28.270 align:middle line:84%
So let's consider
our system to be

00:31:28.270 --> 00:31:32.210 align:middle line:90%
a reservoir at temperature TA.

00:31:32.210 --> 00:31:35.050 align:middle line:90%


00:31:35.050 --> 00:31:38.890 align:middle line:84%
I dropped the subscript 1
because, for a reservoir,

00:31:38.890 --> 00:31:43.600 align:middle line:84%
there is always one
temperature for all states.

00:31:43.600 --> 00:31:46.780 align:middle line:84%
And let's assume that also
system B is a reservoir.

00:31:46.780 --> 00:31:57.490 align:middle line:84%
So also for B here,
I have an equal sign

00:31:57.490 --> 00:32:00.610 align:middle line:84%
because I also assume that
the final states are stable

00:32:00.610 --> 00:32:02.560 align:middle line:90%
equilibrium.

00:32:02.560 --> 00:32:03.140 align:middle line:90%
All right.

00:32:03.140 --> 00:32:06.460 align:middle line:84%
So then either this
or that inequality--

00:32:06.460 --> 00:32:09.050 align:middle line:84%
if the two temperatures
are different--

00:32:09.050 --> 00:32:11.950 align:middle line:84%
and here, we would like
to consider reservoirs

00:32:11.950 --> 00:32:16.820 align:middle line:84%
at different temperatures,
even large differences--

00:32:16.820 --> 00:32:19.840 align:middle line:90%


00:32:19.840 --> 00:32:25.390 align:middle line:84%
there is no way that
this left extreme can

00:32:25.390 --> 00:32:28.090 align:middle line:90%
be equal to the right extreme.

00:32:28.090 --> 00:32:38.200 align:middle line:84%
And therefore, somewhere, there
must be some irreversibility,

00:32:38.200 --> 00:32:42.100 align:middle line:84%
either in system
A or in system B,

00:32:42.100 --> 00:32:51.100 align:middle line:84%
so as to make this train of
equalities and inequalities

00:32:51.100 --> 00:32:52.210 align:middle line:90%
satisfied.

00:32:52.210 --> 00:32:57.830 align:middle line:84%
So it is necessary--
if I transfer energy

00:32:57.830 --> 00:33:00.230 align:middle line:84%
from a reservoir to
another reservoir

00:33:00.230 --> 00:33:02.900 align:middle line:84%
at a different temperature,
it is necessary

00:33:02.900 --> 00:33:08.055 align:middle line:84%
that some entropy be generated
by irreversibility in either one

00:33:08.055 --> 00:33:09.805 align:middle line:84%
because there are no
other systems around.

00:33:09.805 --> 00:33:12.380 align:middle line:90%


00:33:12.380 --> 00:33:22.845 align:middle line:84%
But suppose we interpose a
machinery between that exchange.

00:33:22.845 --> 00:33:25.510 align:middle line:90%


00:33:25.510 --> 00:33:32.770 align:middle line:84%
Well, in that case, it is
possible to have things--

00:33:32.770 --> 00:33:36.610 align:middle line:84%
to operate without
irreversibility,

00:33:36.610 --> 00:33:38.726 align:middle line:90%
so without entropy production.

00:33:38.726 --> 00:33:44.950 align:middle line:90%


00:33:44.950 --> 00:33:49.240 align:middle line:84%
This is the entropy
balance for the machinery.

00:33:49.240 --> 00:33:55.900 align:middle line:84%
It says that, well, if the
machinery produces some entropy

00:33:55.900 --> 00:34:01.060 align:middle line:84%
by irreversibility, it must
be equal to the difference

00:34:01.060 --> 00:34:05.205 align:middle line:84%
between what it puts out
from what it receives.

00:34:05.205 --> 00:34:08.030 align:middle line:90%


00:34:08.030 --> 00:34:11.219 align:middle line:84%
And this is the energy
balance for the machinery.

00:34:11.219 --> 00:34:19.320 align:middle line:84%
It says that it can
produce work if it

00:34:19.320 --> 00:34:28.139 align:middle line:84%
can manage to give to
reservoir B less energy

00:34:28.139 --> 00:34:33.679 align:middle line:84%
than it receives
from reservoir A.

00:34:33.679 --> 00:34:45.540 align:middle line:84%
So we can assume that
everything-- it is

00:34:45.540 --> 00:34:48.120 align:middle line:84%
possible to assume
that everything has

00:34:48.120 --> 00:34:51.480 align:middle line:84%
no entropy produced
by irreversibility,

00:34:51.480 --> 00:34:59.520 align:middle line:84%
so no delta S irr in system,
no delta S irr in system B,

00:34:59.520 --> 00:35:04.350 align:middle line:84%
and also no delta
S irr in system X.

00:35:04.350 --> 00:35:09.010 align:middle line:84%
In that case, from the
entropy point of view,

00:35:09.010 --> 00:35:11.400 align:middle line:84%
the machinery simply
passes the entropy that

00:35:11.400 --> 00:35:17.560 align:middle line:84%
comes from reservoir A and
gives it to reservoir B.

00:35:17.560 --> 00:35:22.900 align:middle line:84%
But it also recognizes that the
machinery is made there just

00:35:22.900 --> 00:35:30.220 align:middle line:84%
to recognize that, in order to
pass that entropy to system B,

00:35:30.220 --> 00:35:34.000 align:middle line:84%
it doesn't need to give it
all the energy it received

00:35:34.000 --> 00:35:42.100 align:middle line:84%
from A. There is an unbalance,
the difference, which can be

00:35:42.100 --> 00:35:47.290 align:middle line:84%
transferred out by means of
an interaction in which there

00:35:47.290 --> 00:35:49.245 align:middle line:90%
is no entropy transfer, work.

00:35:49.245 --> 00:35:52.790 align:middle line:90%


00:35:52.790 --> 00:36:02.430 align:middle line:84%
OK, so that's the idea of
the heat engine, machinery

00:36:02.430 --> 00:36:06.700 align:middle line:84%
that receives heat from a
reservoir at high temperature.

00:36:06.700 --> 00:36:09.270 align:middle line:84%
This is a heat engine between
thermal reservoirs because you

00:36:09.270 --> 00:36:12.120 align:middle line:84%
could have also heat
engines between systems

00:36:12.120 --> 00:36:14.910 align:middle line:90%
that are not reservoirs.

00:36:14.910 --> 00:36:21.910 align:middle line:84%
I take a big piece of steel
out of a steelmaking plant.

00:36:21.910 --> 00:36:24.660 align:middle line:84%
And I want to recuperate
the energy that it

00:36:24.660 --> 00:36:27.060 align:middle line:90%
has before it cools down.

00:36:27.060 --> 00:36:33.390 align:middle line:84%
That's a way of
recovering energy

00:36:33.390 --> 00:36:34.990 align:middle line:90%
from industrial processes.

00:36:34.990 --> 00:36:39.660 align:middle line:84%
And of course, as I call
it down, the piece of steel

00:36:39.660 --> 00:36:41.590 align:middle line:90%
decreases its temperature.

00:36:41.590 --> 00:36:45.470 align:middle line:90%
And so it's not a reservoir.

00:36:45.470 --> 00:36:49.620 align:middle line:84%
That doesn't mean we cannot
compute also for that situation

00:36:49.620 --> 00:36:52.680 align:middle line:84%
what is the maximum work
that we can extract.

00:36:52.680 --> 00:36:56.660 align:middle line:90%
But that's another situation.

00:36:56.660 --> 00:36:58.490 align:middle line:84%
And for example,
the maximum work

00:36:58.490 --> 00:37:04.850 align:middle line:84%
we can extract in that case
is not the Carnot coefficient.

00:37:04.850 --> 00:37:09.030 align:middle line:84%
Whereas here, if you do
energy and entropy balance--

00:37:09.030 --> 00:37:11.090 align:middle line:90%
and here they are.

00:37:11.090 --> 00:37:13.530 align:middle line:90%
I'm going quickly here.

00:37:13.530 --> 00:37:15.620 align:middle line:84%
And I'm not going
too into the details,

00:37:15.620 --> 00:37:19.640 align:middle line:84%
just give you some
ideas by following

00:37:19.640 --> 00:37:21.650 align:middle line:90%
the flows of the entropy.

00:37:21.650 --> 00:37:25.430 align:middle line:84%
But here are the full
glory of the balance

00:37:25.430 --> 00:37:33.110 align:middle line:84%
equations for the
machinery, from which

00:37:33.110 --> 00:37:36.235 align:middle line:90%
you can compute the work.

00:37:36.235 --> 00:37:38.990 align:middle line:90%


00:37:38.990 --> 00:37:42.650 align:middle line:84%
Here is the result. So the work
that the machinery-- the useful

00:37:42.650 --> 00:37:44.790 align:middle line:84%
effect that the
machinery can produce

00:37:44.790 --> 00:37:49.980 align:middle line:84%
is equal to a
fraction of the heat

00:37:49.980 --> 00:37:52.650 align:middle line:84%
that it receives from
the hot reservoir.

00:37:52.650 --> 00:37:56.820 align:middle line:84%
And that fraction is
the Carnot coefficient

00:37:56.820 --> 00:38:00.950 align:middle line:90%
between those two temperatures.

00:38:00.950 --> 00:38:05.790 align:middle line:84%
And then there is also
a term which detracts.

00:38:05.790 --> 00:38:07.820 align:middle line:84%
And that is proportional
to the entropy

00:38:07.820 --> 00:38:09.320 align:middle line:84%
that is produced
by irreversibility

00:38:09.320 --> 00:38:11.600 align:middle line:90%
within the machinery.

00:38:11.600 --> 00:38:12.840 align:middle line:90%
It has a minus sign.

00:38:12.840 --> 00:38:17.420 align:middle line:84%
So if the machinery
does produce entropy,

00:38:17.420 --> 00:38:21.080 align:middle line:84%
that will detract and
will allow you to get

00:38:21.080 --> 00:38:23.065 align:middle line:90%
less work than the maximum.

00:38:23.065 --> 00:38:34.630 align:middle line:90%


00:38:34.630 --> 00:38:40.630 align:middle line:84%
Let's view it from the point
of view of entropy flows.

00:38:40.630 --> 00:38:49.960 align:middle line:84%
Actually, maybe
we can also do it

00:38:49.960 --> 00:38:54.690 align:middle line:90%
in terms of E versus S diagrams.

00:38:54.690 --> 00:38:58.850 align:middle line:90%


00:38:58.850 --> 00:39:06.680 align:middle line:84%
So this is system A, reservoir
A. And this is reservoir B.

00:39:06.680 --> 00:39:09.770 align:middle line:90%
And I'm extracting some energy.

00:39:09.770 --> 00:39:25.830 align:middle line:84%
So I want to take this much
energy out of system A.

00:39:25.830 --> 00:39:28.810 align:middle line:84%
Clearly, there are
no states here.

00:39:28.810 --> 00:39:34.565 align:middle line:84%
So I need to extract also some
entropy, at least this much.

00:39:34.565 --> 00:39:37.380 align:middle line:90%


00:39:37.380 --> 00:39:42.730 align:middle line:84%
But in order to extract that
entropy, I need another system--

00:39:42.730 --> 00:39:46.260 align:middle line:84%
that's why I need
the reservoir B--

00:39:46.260 --> 00:39:52.000 align:middle line:90%
that picks up that entropy.

00:39:52.000 --> 00:39:53.550 align:middle line:90%
And so it will end up here.

00:39:53.550 --> 00:39:59.050 align:middle line:90%


00:39:59.050 --> 00:40:03.280 align:middle line:90%
It will end up here, provided--

00:40:03.280 --> 00:40:06.850 align:middle line:84%
since there are no states to the
right of the maximum entropy,

00:40:06.850 --> 00:40:08.840 align:middle line:84%
I need also to
provide some energy.

00:40:08.840 --> 00:40:12.730 align:middle line:90%
And that energy is this much.

00:40:12.730 --> 00:40:24.850 align:middle line:84%
It's Q received by B. So the
difference between this and that

00:40:24.850 --> 00:40:25.825 align:middle line:90%
is the work.

00:40:25.825 --> 00:40:29.230 align:middle line:90%


00:40:29.230 --> 00:40:37.540 align:middle line:84%
If I draw a line with the
slope of reservoir A here,

00:40:37.540 --> 00:40:43.970 align:middle line:84%
this is the work that
I have extracted.

00:40:43.970 --> 00:40:47.380 align:middle line:84%
Actually, this is
W rev because I

00:40:47.380 --> 00:40:55.810 align:middle line:84%
have assumed that system B
takes just barely the entropy

00:40:55.810 --> 00:40:57.940 align:middle line:90%
that we need to--

00:40:57.940 --> 00:41:02.140 align:middle line:84%
that is being received by
system A. So it flows--

00:41:02.140 --> 00:41:08.795 align:middle line:84%
the entropy comes from
A. The machinery doesn't

00:41:08.795 --> 00:41:11.480 align:middle line:84%
add because it's
reversible, it doesn't

00:41:11.480 --> 00:41:13.200 align:middle line:90%
produce additional entropy.

00:41:13.200 --> 00:41:20.570 align:middle line:84%
It simply has to
transfer it to system B.

00:41:20.570 --> 00:41:29.000 align:middle line:84%
And the energy that is required
to transfer that to system B

00:41:29.000 --> 00:41:31.020 align:middle line:90%
is less than QA.

00:41:31.020 --> 00:41:32.790 align:middle line:84%
And therefore, there
is a difference.

00:41:32.790 --> 00:41:35.900 align:middle line:84%
And that difference
can be transferred

00:41:35.900 --> 00:41:39.110 align:middle line:84%
in an interaction where there
is no entropy transfer, which

00:41:39.110 --> 00:41:40.280 align:middle line:90%
is work.

00:41:40.280 --> 00:41:43.260 align:middle line:84%
So this is the
reversible operation.

00:41:43.260 --> 00:41:46.710 align:middle line:84%
If we have an
irreversible operation,

00:41:46.710 --> 00:41:49.045 align:middle line:84%
so if the machinery
is irreversible,

00:41:49.045 --> 00:41:52.580 align:middle line:84%
like most practical
machineries, and therefore it

00:41:52.580 --> 00:41:55.670 align:middle line:84%
produces some entropy,
that entropy will also

00:41:55.670 --> 00:42:01.880 align:middle line:84%
need to be disposed of into
the environmental reservoir.

00:42:01.880 --> 00:42:09.780 align:middle line:84%
And therefore, it will
require more energy to follow.

00:42:09.780 --> 00:42:14.790 align:middle line:84%
So in the system B, I need
to add not only this entropy,

00:42:14.790 --> 00:42:19.240 align:middle line:84%
but also the entropy that is
produced by irreversibility.

00:42:19.240 --> 00:42:23.220 align:middle line:84%
So that is S irr produced
in the machinery.

00:42:23.220 --> 00:42:29.975 align:middle line:84%
And the machinery is called
M. So system B ends up here.

00:42:29.975 --> 00:42:34.120 align:middle line:90%


00:42:34.120 --> 00:42:39.820 align:middle line:90%
The amount of Q is higher.

00:42:39.820 --> 00:42:46.300 align:middle line:84%
And therefore, the amount
left, the difference,

00:42:46.300 --> 00:42:50.910 align:middle line:84%
which is what will be
transferred as work, is less.

00:42:50.910 --> 00:42:55.420 align:middle line:90%


00:42:55.420 --> 00:42:57.610 align:middle line:90%
Good.

00:42:57.610 --> 00:43:00.410 align:middle line:84%
So we have seen it
in various ways.

00:43:00.410 --> 00:43:03.966 align:middle line:84%
Now, typically, one
defines the efficiency.

00:43:03.966 --> 00:43:07.170 align:middle line:90%


00:43:07.170 --> 00:43:14.070 align:middle line:84%
Actually, most of
you probably remember

00:43:14.070 --> 00:43:19.080 align:middle line:84%
that this ratio is not called
the Carnot coefficient,

00:43:19.080 --> 00:43:20.140 align:middle line:90%
like I'm calling it.

00:43:20.140 --> 00:43:23.580 align:middle line:84%
But it's called
Carnot efficiency,

00:43:23.580 --> 00:43:30.720 align:middle line:84%
which is true in the sense that
I can define an efficiency--

00:43:30.720 --> 00:43:33.756 align:middle line:84%
we are going to call it
here first-law efficiency--

00:43:33.756 --> 00:43:36.490 align:middle line:90%


00:43:36.490 --> 00:43:38.570 align:middle line:84%
as the ratio of
the useful work--

00:43:38.570 --> 00:43:46.180 align:middle line:84%
so the work-- divided by
the energy of the resource

00:43:46.180 --> 00:43:47.420 align:middle line:90%
that you have used.

00:43:47.420 --> 00:43:50.680 align:middle line:84%
In this case, the resource
is the hot reservoir,

00:43:50.680 --> 00:43:53.050 align:middle line:84%
so the energy extracted
from the hot reservoir.

00:43:53.050 --> 00:43:58.720 align:middle line:84%
So this ratio is the
first-law efficiency.

00:43:58.720 --> 00:44:01.150 align:middle line:84%
And the result of the
energy and entropy balance

00:44:01.150 --> 00:44:06.460 align:middle line:84%
shows that the
Carnot coefficient

00:44:06.460 --> 00:44:12.400 align:middle line:84%
is the upper limit of this
efficiency, which is reached

00:44:12.400 --> 00:44:15.610 align:middle line:90%
when S here is equal to 0.

00:44:15.610 --> 00:44:20.290 align:middle line:84%
So the Carnot coefficient
is equal to the first law

00:44:20.290 --> 00:44:23.610 align:middle line:84%
efficiency for the
reversible engine.

00:44:23.610 --> 00:44:27.990 align:middle line:90%


00:44:27.990 --> 00:44:39.360 align:middle line:84%
What is somehow inconvenient
of first-law efficiencies

00:44:39.360 --> 00:44:48.870 align:middle line:84%
is that usually when you say,
something is 50% efficient,

00:44:48.870 --> 00:44:52.620 align:middle line:84%
I would say, well, why
aren't you doing better?

00:44:52.620 --> 00:44:56.260 align:middle line:84%
There is 50% room
for improvement.

00:44:56.260 --> 00:44:59.490 align:middle line:90%


00:44:59.490 --> 00:45:03.540 align:middle line:84%
Not here though, because
there is no way--

00:45:03.540 --> 00:45:09.760 align:middle line:84%
suppose you have TA is equal
to 600K and TB is 300K.

00:45:09.760 --> 00:45:12.960 align:middle line:84%
So the Carnot
coefficient is 1/2,

00:45:12.960 --> 00:45:16.990 align:middle line:84%
50% That's the
maximum you can do.

00:45:16.990 --> 00:45:19.060 align:middle line:90%
There is no improvement.

00:45:19.060 --> 00:45:21.840 align:middle line:90%
You cannot improve.

00:45:21.840 --> 00:45:29.210 align:middle line:84%
So it would be better to have
to call efficiency or to--

00:45:29.210 --> 00:45:31.980 align:middle line:84%
so people have introduced
the second-law efficiency,

00:45:31.980 --> 00:45:37.460 align:middle line:84%
which compares what you
actually obtained and put it

00:45:37.460 --> 00:45:42.470 align:middle line:84%
in a numerator to the maximum
that you could have obtained,

00:45:42.470 --> 00:45:46.340 align:middle line:84%
given the constraints
and the physical laws,

00:45:46.340 --> 00:45:47.875 align:middle line:90%
so without violating anything.

00:45:47.875 --> 00:45:50.990 align:middle line:90%


00:45:50.990 --> 00:45:57.180 align:middle line:84%
So in that case, this ratio,
for the reversible case, is 1.

00:45:57.180 --> 00:46:03.810 align:middle line:84%
So it's 100% And so if
the efficiency is 100%,

00:46:03.810 --> 00:46:05.370 align:middle line:90%
there's no room for improvement.

00:46:05.370 --> 00:46:08.940 align:middle line:90%


00:46:08.940 --> 00:46:16.170 align:middle line:84%
If it is not 100% or
1, it means that there

00:46:16.170 --> 00:46:19.320 align:middle line:90%
is something that reduces that.

00:46:19.320 --> 00:46:22.950 align:middle line:84%
And that something
is the entropy

00:46:22.950 --> 00:46:24.610 align:middle line:90%
produced by irreversibility.

00:46:24.610 --> 00:46:31.440 align:middle line:84%
So by thinking in these terms,
this second-law efficiency

00:46:31.440 --> 00:46:42.960 align:middle line:84%
allows you to identify the
actual places in your machinery

00:46:42.960 --> 00:46:52.140 align:middle line:84%
or power plant that are the
sites where entropy gets

00:46:52.140 --> 00:46:56.340 align:middle line:84%
produced by irreversibility
because the higher the entropy

00:46:56.340 --> 00:47:00.220 align:middle line:84%
produced by irreversibility,
the lesser this efficiency,

00:47:00.220 --> 00:47:03.780 align:middle line:84%
so the more room
for improvement.

00:47:03.780 --> 00:47:10.300 align:middle line:84%
And in fact, a lot of energy
technology engineering

00:47:10.300 --> 00:47:16.070 align:middle line:84%
is into improving
this efficiency.

00:47:16.070 --> 00:47:19.240 align:middle line:84%
That means identifying where
the irreversibilities are

00:47:19.240 --> 00:47:22.580 align:middle line:84%
and removing them or
reducing them, optimizing

00:47:22.580 --> 00:47:23.580 align:middle line:90%
from that point of view.

00:47:23.580 --> 00:47:28.256 align:middle line:90%


00:47:28.256 --> 00:47:36.930 align:middle line:84%
So let's do, even more
quickly, the same idea,

00:47:36.930 --> 00:47:38.695 align:middle line:90%
but for a refrigerator unit.

00:47:38.695 --> 00:47:41.250 align:middle line:90%


00:47:41.250 --> 00:47:44.970 align:middle line:84%
It's again a situation in
which I have two reservoirs, TA

00:47:44.970 --> 00:47:47.130 align:middle line:90%
and TB.

00:47:47.130 --> 00:47:58.015 align:middle line:84%
And I identify the
environment as the system

00:47:58.015 --> 00:47:59.760 align:middle line:90%
at a higher temperature now.

00:47:59.760 --> 00:48:02.740 align:middle line:90%


00:48:02.740 --> 00:48:09.460 align:middle line:84%
And the other system,
at the lower temperature

00:48:09.460 --> 00:48:16.270 align:middle line:84%
is, for example, the
refrigerator cell, the room

00:48:16.270 --> 00:48:18.530 align:middle line:84%
that you want to
keep refrigerated.

00:48:18.530 --> 00:48:21.620 align:middle line:84%
And you want to keep
it refrigerated.

00:48:21.620 --> 00:48:25.810 align:middle line:84%
So since typically
there are heat losses

00:48:25.810 --> 00:48:29.720 align:middle line:84%
from the walls of
this refrigerator,

00:48:29.720 --> 00:48:34.060 align:middle line:84%
you need to compensate
by removing heat.

00:48:34.060 --> 00:48:39.550 align:middle line:84%
So the unit wants to extract
heat from a low temperature,

00:48:39.550 --> 00:48:41.530 align:middle line:84%
from a temperature
from a reservoir which

00:48:41.530 --> 00:48:44.266 align:middle line:84%
is at lower temperature
than the environment.

00:48:44.266 --> 00:48:49.050 align:middle line:90%


00:48:49.050 --> 00:48:50.915 align:middle line:90%
So if we go on our--

00:48:50.915 --> 00:48:56.390 align:middle line:90%


00:48:56.390 --> 00:49:04.790 align:middle line:84%
do again the
construction here, now I

00:49:04.790 --> 00:49:12.320 align:middle line:84%
want my system B, which
is the refrigerated room--

00:49:12.320 --> 00:49:18.560 align:middle line:90%
you want to extract energy.

00:49:18.560 --> 00:49:22.710 align:middle line:84%
And as usual, in order
to extract energy,

00:49:22.710 --> 00:49:25.010 align:middle line:84%
you need to extract
also entropy.

00:49:25.010 --> 00:49:28.130 align:middle line:90%
So this is QB out.

00:49:28.130 --> 00:49:37.510 align:middle line:90%
And this is SB out.

00:49:37.510 --> 00:49:43.280 align:middle line:84%
So if I have this
entropy going somewhere,

00:49:43.280 --> 00:49:46.515 align:middle line:84%
I need to put it
to another system.

00:49:46.515 --> 00:49:50.400 align:middle line:90%


00:49:50.400 --> 00:49:57.850 align:middle line:84%
Now, this system A, which
is my environment, is there.

00:49:57.850 --> 00:50:07.680 align:middle line:84%
And I would like to give
it this much entropy.

00:50:07.680 --> 00:50:11.310 align:middle line:84%
But in order to
give it, I also need

00:50:11.310 --> 00:50:21.070 align:middle line:84%
to give some energy, which is
actually higher than this one

00:50:21.070 --> 00:50:25.880 align:middle line:84%
because the
environment is hotter.

00:50:25.880 --> 00:50:27.490 align:middle line:90%
So it has a higher slope.

00:50:27.490 --> 00:50:36.200 align:middle line:84%
So if I plot here the
slope of system B,

00:50:36.200 --> 00:50:45.995 align:middle line:84%
this is the energy that
I extract from system B.

00:50:45.995 --> 00:50:49.940 align:middle line:84%
But I need to give to
A more energy in order

00:50:49.940 --> 00:50:52.280 align:middle line:84%
for it to accommodate
the entropy that I

00:50:52.280 --> 00:50:59.060 align:middle line:84%
must extract from B. So
this much is the work

00:50:59.060 --> 00:51:00.385 align:middle line:90%
that I need to spend.

00:51:00.385 --> 00:51:10.345 align:middle line:90%


00:51:10.345 --> 00:51:14.380 align:middle line:84%
And of course, if the
machinery is irreversible

00:51:14.380 --> 00:51:17.420 align:middle line:84%
and it produces also some
entropy by irreversibility,

00:51:17.420 --> 00:51:21.580 align:middle line:84%
not only I must accommodate
this much entropy,

00:51:21.580 --> 00:51:25.630 align:middle line:84%
but I must
accommodate even more.

00:51:25.630 --> 00:51:34.400 align:middle line:84%
That's the irreversibility
of the machinery, this much.

00:51:34.400 --> 00:51:36.860 align:middle line:90%
So system A must go up there.

00:51:36.860 --> 00:51:40.650 align:middle line:84%
And therefore, I need
to spend more work.

00:51:40.650 --> 00:51:49.590 align:middle line:84%
So this was W rev. And this
match is W, say, irreversible.

00:51:49.590 --> 00:51:55.191 align:middle line:90%


00:51:55.191 --> 00:52:03.030 align:middle line:84%
Now also here, the Carnot
coefficient or similar

00:52:03.030 --> 00:52:06.900 align:middle line:90%
does play a role.

00:52:06.900 --> 00:52:11.010 align:middle line:84%
Usually, in practice, when
you buy a refrigerator,

00:52:11.010 --> 00:52:17.760 align:middle line:84%
you want to know what the COP,
the coefficient of performance,

00:52:17.760 --> 00:52:21.240 align:middle line:90%
is, which is a first-law ratio.

00:52:21.240 --> 00:52:26.280 align:middle line:84%
It's the ratio of the useful,
the cooling effect, which

00:52:26.280 --> 00:52:30.780 align:middle line:84%
is the energy you extract
from the low temperature cell,

00:52:30.780 --> 00:52:35.760 align:middle line:84%
to the work, typically
electrical work,

00:52:35.760 --> 00:52:41.375 align:middle line:84%
that you need to spend
in order to do this.

00:52:41.375 --> 00:52:46.130 align:middle line:90%


00:52:46.130 --> 00:52:54.530 align:middle line:84%
And this COP has
a highest value.

00:52:54.530 --> 00:52:57.930 align:middle line:84%
And then there is a term,
which is always positive.

00:52:57.930 --> 00:53:03.630 align:middle line:84%
And that is bigger
and bigger the more

00:53:03.630 --> 00:53:05.460 align:middle line:90%
irreversible is your machinery.

00:53:05.460 --> 00:53:09.938 align:middle line:90%


00:53:09.938 --> 00:53:15.365 align:middle line:84%
Also here, COP is typically
a number greater than 1.

00:53:15.365 --> 00:53:18.322 align:middle line:90%


00:53:18.322 --> 00:53:21.680 align:middle line:84%
It doesn't give you
an indication of what

00:53:21.680 --> 00:53:26.510 align:middle line:90%
the room for improvement is.

00:53:26.510 --> 00:53:31.250 align:middle line:84%
The second-law
efficiency instead does.

00:53:31.250 --> 00:53:37.730 align:middle line:84%
And again, we can define it as
the actual useful effect divided

00:53:37.730 --> 00:53:44.780 align:middle line:84%
by the best useful effect,
the maximum useful effect you

00:53:44.780 --> 00:53:49.870 align:middle line:84%
could obtain with a
reversible machinery.

00:53:49.870 --> 00:53:58.570 align:middle line:84%
That too has a maximum
value equal to 100%.

00:53:58.570 --> 00:54:01.180 align:middle line:84%
In that case, there is
no room for improvement.

00:54:01.180 --> 00:54:03.740 align:middle line:90%


00:54:03.740 --> 00:54:07.630 align:middle line:84%
And it's less than 1, due
to the entropy produced

00:54:07.630 --> 00:54:08.870 align:middle line:90%
by irreversibility.

00:54:08.870 --> 00:54:12.700 align:middle line:90%


00:54:12.700 --> 00:54:22.330 align:middle line:84%
The last of this series
of traditional machineries

00:54:22.330 --> 00:54:25.360 align:middle line:90%
is the heat pump.

00:54:25.360 --> 00:54:29.950 align:middle line:84%
The heat pump is very similar
to a refrigerator, more or less

00:54:29.950 --> 00:54:36.190 align:middle line:84%
the same equations, except
that now what switches

00:54:36.190 --> 00:54:39.010 align:middle line:84%
is the position of
the environment,

00:54:39.010 --> 00:54:43.000 align:middle line:84%
of your environment, the
environmental reservoir.

00:54:43.000 --> 00:54:50.530 align:middle line:84%
Whereas for the refrigerator
you were extracting energy

00:54:50.530 --> 00:54:53.830 align:middle line:84%
from something which is
colder than the environment,

00:54:53.830 --> 00:54:58.900 align:middle line:84%
in the heat pump, you
want to put energy

00:54:58.900 --> 00:55:03.650 align:middle line:84%
in a reservoir which is
hotter than the environment.

00:55:03.650 --> 00:55:06.230 align:middle line:90%


00:55:06.230 --> 00:55:10.760 align:middle line:84%
So now, the environment
is system B.

00:55:10.760 --> 00:55:16.100 align:middle line:84%
But the idea is more
or less the same,

00:55:16.100 --> 00:55:20.570 align:middle line:84%
except that the useful effect
now is not the cooling of B,

00:55:20.570 --> 00:55:23.960 align:middle line:84%
but is the heating of A. You
want to heat up something,

00:55:23.960 --> 00:55:28.470 align:middle line:84%
like the house,
using a heat pump,

00:55:28.470 --> 00:55:33.140 align:middle line:84%
which is nowadays
been done worldwide,

00:55:33.140 --> 00:55:38.310 align:middle line:84%
at least in places where you
need heating in the winter time.

00:55:38.310 --> 00:55:43.490 align:middle line:90%
And so the useful effect is QA.

00:55:43.490 --> 00:55:46.520 align:middle line:84%
Therefore, you define
a different COP.

00:55:46.520 --> 00:55:49.460 align:middle line:84%
It's called COP,
but it's different,

00:55:49.460 --> 00:55:51.026 align:middle line:90%
a different definition.

00:55:51.026 --> 00:55:54.110 align:middle line:90%


00:55:54.110 --> 00:56:00.830 align:middle line:84%
And this time, you
put in the numerator

00:56:00.830 --> 00:56:06.470 align:middle line:84%
the useful effect,
which is the heat given

00:56:06.470 --> 00:56:13.850 align:middle line:84%
to the hot system
divided by the work

00:56:13.850 --> 00:56:19.020 align:middle line:84%
that you have spent
in order to do it.

00:56:19.020 --> 00:56:25.040 align:middle line:84%
And again, the
second-law efficiency

00:56:25.040 --> 00:56:31.970 align:middle line:84%
is the ratio between the useful
effect of your actual machinery

00:56:31.970 --> 00:56:35.180 align:middle line:84%
and the useful effect of
the reversible machinery,

00:56:35.180 --> 00:56:40.920 align:middle line:84%
so that it would be equal to
1 for a reversible machinery.

00:56:40.920 --> 00:56:44.360 align:middle line:84%
And it's less than 1 if
there is entropy produced

00:56:44.360 --> 00:56:46.750 align:middle line:90%
by your machinery here.

00:56:46.750 --> 00:56:56.239 align:middle line:90%


00:56:56.239 --> 00:57:04.740 align:middle line:84%
So since now we are talking
about some practical aspects,

00:57:04.740 --> 00:57:12.930 align:middle line:84%
let's talk about another
chapter of thermodynamics that

00:57:12.930 --> 00:57:17.250 align:middle line:84%
has to do with establishing
the properties of substances

00:57:17.250 --> 00:57:20.250 align:middle line:90%
at stable equilibrium.

00:57:20.250 --> 00:57:22.880 align:middle line:84%
And let's see, this is
an important chapter.

00:57:22.880 --> 00:57:27.660 align:middle line:90%


00:57:27.660 --> 00:57:31.050 align:middle line:84%
Many scientists have
devoted their lives

00:57:31.050 --> 00:57:35.016 align:middle line:84%
in constructing the
properties of substances.

00:57:35.016 --> 00:57:38.770 align:middle line:90%


00:57:38.770 --> 00:57:51.230 align:middle line:84%
For example, to stay
here, Professor Keenan,

00:57:51.230 --> 00:57:57.650 align:middle line:84%
in 1940 or maybe
earlier, spent a lot

00:57:57.650 --> 00:58:01.130 align:middle line:84%
of time developing the
steam tables, which

00:58:01.130 --> 00:58:05.910 align:middle line:90%
is the properties of water.

00:58:05.910 --> 00:58:09.500 align:middle line:84%
So how do we measure
properties of substances

00:58:09.500 --> 00:58:11.280 align:middle line:90%
in stable equilibrium?

00:58:11.280 --> 00:58:15.580 align:middle line:90%


00:58:15.580 --> 00:58:22.180 align:middle line:84%
Well, much of the
tools that we have

00:58:22.180 --> 00:58:28.060 align:middle line:84%
is related to the conditions
for mutual stable equilibrium

00:58:28.060 --> 00:58:33.050 align:middle line:84%
that we have developed, like
equality of temperature,

00:58:33.050 --> 00:58:38.830 align:middle line:84%
equality of pressure, equality
of chemical potentials.

00:58:38.830 --> 00:58:42.680 align:middle line:84%
The good thing is that, if
you have a thermometer--

00:58:42.680 --> 00:58:45.700 align:middle line:90%


00:58:45.700 --> 00:58:46.840 align:middle line:90%
what is a thermometer?

00:58:46.840 --> 00:58:52.030 align:middle line:84%
A thermometer is a system
in which, in some way,

00:58:52.030 --> 00:58:58.720 align:middle line:84%
you have put a scale
in which you can read

00:58:58.720 --> 00:59:01.700 align:middle line:90%
the value of the temperature.

00:59:01.700 --> 00:59:04.660 align:middle line:84%
Then what you do, you
stick it in contact

00:59:04.660 --> 00:59:07.230 align:middle line:84%
to the system you
want to measure.

00:59:07.230 --> 00:59:11.750 align:middle line:90%


00:59:11.750 --> 00:59:18.350 align:middle line:84%
And you leave enough time so
that you convince yourself

00:59:18.350 --> 00:59:21.360 align:middle line:84%
that the two systems have
reached mutual equilibrium.

00:59:21.360 --> 00:59:24.000 align:middle line:84%
And if you are convinced that
they are in mutual equilibrium,

00:59:24.000 --> 00:59:27.210 align:middle line:84%
then the theory says that the
two temperatures are equal.

00:59:27.210 --> 00:59:33.600 align:middle line:84%
So by reading the temperature
of the thermometer,

00:59:33.600 --> 00:59:36.245 align:middle line:84%
you have measured the
temperature of system A,

00:59:36.245 --> 00:59:39.230 align:middle line:90%
of which you may know nothing.

00:59:39.230 --> 00:59:43.975 align:middle line:84%
So it's an indirect
measurement of a property.

00:59:43.975 --> 00:59:46.740 align:middle line:90%


00:59:46.740 --> 00:59:54.000 align:middle line:84%
Similarly, the manometer--
you can construct a manometer

00:59:54.000 --> 00:59:59.040 align:middle line:84%
so that you can read out
the scale, the value here.

00:59:59.040 --> 01:00:03.720 align:middle line:84%
You put it in equilibrium,
mutual equilibrium

01:00:03.720 --> 01:00:11.550 align:middle line:84%
with your system by drilling
a little hole in the boundary

01:00:11.550 --> 01:00:18.930 align:middle line:84%
with either a little piston
or some moving interface,

01:00:18.930 --> 01:00:19.680 align:middle line:90%
like here.

01:00:19.680 --> 01:00:25.410 align:middle line:90%


01:00:25.410 --> 01:00:28.500 align:middle line:84%
If you are convinced that they
are in mutual equilibrium,

01:00:28.500 --> 01:00:30.750 align:middle line:84%
reading the pressure
of B gives you

01:00:30.750 --> 01:00:34.410 align:middle line:84%
information about the
pressure of system A.

01:00:34.410 --> 01:00:40.430 align:middle line:84%
So this is one way
of measuring it.

01:00:40.430 --> 01:00:47.460 align:middle line:84%
Yeah, this is just to
remind of that proof

01:00:47.460 --> 01:00:53.420 align:middle line:84%
that I don't want to
go into details of,

01:00:53.420 --> 01:01:02.610 align:middle line:84%
but that shows why the
pressure can be measured

01:01:02.610 --> 01:01:07.900 align:middle line:84%
by measuring a
force per unit area

01:01:07.900 --> 01:01:13.910 align:middle line:84%
anywhere on the
boundary of your system.

01:01:13.910 --> 01:01:15.680 align:middle line:84%
So you take the
boundary of your system

01:01:15.680 --> 01:01:19.840 align:middle line:84%
when it is in stable
equilibrium, drill a hole,

01:01:19.840 --> 01:01:24.640 align:middle line:84%
and substitute that piece of
wall with the movable wall.

01:01:24.640 --> 01:01:28.510 align:middle line:84%
And then you find a
force per unit area

01:01:28.510 --> 01:01:31.790 align:middle line:84%
that keeps that wall where
the original one was.

01:01:31.790 --> 01:01:36.020 align:middle line:84%
Once you've found that, you have
measured the force per unit area

01:01:36.020 --> 01:01:41.020 align:middle line:84%
that balances the
pressure of your system.

01:01:41.020 --> 01:01:43.220 align:middle line:84%
And when you are in
stable equilibrium,

01:01:43.220 --> 01:01:45.850 align:middle line:84%
that force per unit
area is equal no matter

01:01:45.850 --> 01:01:50.560 align:middle line:84%
where you go and
do this procedure,

01:01:50.560 --> 01:01:56.770 align:middle line:84%
whereas off
equilibrium, it can be--

01:01:56.770 --> 01:02:00.050 align:middle line:84%
you can always measure
force per unit area.

01:02:00.050 --> 01:02:06.590 align:middle line:84%
But it may be non-uniform,
not equal everywhere.

01:02:06.590 --> 01:02:09.480 align:middle line:84%
And there is no pressure because
you are not in equilibrium.

01:02:09.480 --> 01:02:14.880 align:middle line:90%


01:02:14.880 --> 01:02:26.610 align:middle line:84%
Another kind of measurement that
we can do is the so-called Joule

01:02:26.610 --> 01:02:33.300 align:middle line:84%
apparatus, in which you
input some mechanical energy

01:02:33.300 --> 01:02:38.820 align:middle line:84%
in your substance,
or in a piston--

01:02:38.820 --> 01:02:44.910 align:middle line:84%
or in a variable volume, or in
a constant volume container.

01:02:44.910 --> 01:02:50.610 align:middle line:84%
You put some energy
in, wait for the system

01:02:50.610 --> 01:02:53.310 align:middle line:84%
to go to a new
stable equilibrium,

01:02:53.310 --> 01:03:03.960 align:middle line:84%
and measure how
much the temperature

01:03:03.960 --> 01:03:07.110 align:middle line:90%
has changed for your system.

01:03:07.110 --> 01:03:14.310 align:middle line:84%
So Mg delta z represents
the amount of energy

01:03:14.310 --> 01:03:17.340 align:middle line:84%
that you have put in,
in the form of work.

01:03:17.340 --> 01:03:20.010 align:middle line:84%
So you produce a
work interaction

01:03:20.010 --> 01:03:23.850 align:middle line:84%
and put energy into
your system, let

01:03:23.850 --> 01:03:27.580 align:middle line:84%
it relax until it
reaches equilibrium, so

01:03:27.580 --> 01:03:30.240 align:middle line:84%
a new temperature,
compute the difference

01:03:30.240 --> 01:03:32.830 align:middle line:84%
between the new temperature
and the initial temperature,

01:03:32.830 --> 01:03:36.750 align:middle line:84%
delta T. This ratio
turns out to be

01:03:36.750 --> 01:03:39.990 align:middle line:84%
equal to the partial
derivative of this property

01:03:39.990 --> 01:03:44.530 align:middle line:84%
that we're going to
define in a moment.

01:03:44.530 --> 01:03:47.970 align:middle line:84%
And that's the property
that we call heat capacity

01:03:47.970 --> 01:03:49.750 align:middle line:90%
at constant pressure.

01:03:49.750 --> 01:03:52.500 align:middle line:84%
It's a stable equilibrium
state property.

01:03:52.500 --> 01:03:54.680 align:middle line:84%
We obtain it from the
fundamental relation.

01:03:54.680 --> 01:03:58.110 align:middle line:90%


01:03:58.110 --> 01:04:04.720 align:middle line:84%
There is one heat capacity
that is equal to the same ratio

01:04:04.720 --> 01:04:07.530 align:middle line:84%
when you do the experiment
at constant volume.

01:04:07.530 --> 01:04:10.140 align:middle line:84%
And there is another
heat capacity when

01:04:10.140 --> 01:04:12.410 align:middle line:90%
you do it at constant pressure.

01:04:12.410 --> 01:04:17.160 align:middle line:90%


01:04:17.160 --> 01:04:19.500 align:middle line:84%
So let's start from
the constant pressure

01:04:19.500 --> 01:04:31.220 align:middle line:84%
because this gives us also a
procedure to define the enthalpy

01:04:31.220 --> 01:04:38.560 align:middle line:84%
and to get to this, the
derivative that turns out

01:04:38.560 --> 01:04:41.270 align:middle line:84%
to represent the result
of these measurements.

01:04:41.270 --> 01:04:44.470 align:middle line:84%
So it's important because
it is the way in which you

01:04:44.470 --> 01:04:45.720 align:middle line:90%
measure that property.

01:04:45.720 --> 01:04:50.660 align:middle line:90%


01:04:50.660 --> 01:04:55.280 align:middle line:84%
Let's do it starting from
the fundamental relation

01:04:55.280 --> 01:04:58.160 align:middle line:90%
in energy form.

01:04:58.160 --> 01:05:00.750 align:middle line:90%
And this is its differential.

01:05:00.750 --> 01:05:03.600 align:middle line:90%


01:05:03.600 --> 01:05:12.410 align:middle line:84%
So H-- in a moment, we
will see that this H has

01:05:12.410 --> 01:05:18.500 align:middle line:84%
a particular transform of
the fundamental relation when

01:05:18.500 --> 01:05:19.410 align:middle line:90%
we change variables.

01:05:19.410 --> 01:05:25.530 align:middle line:84%
But for the moment, let's just
take it as an abrupt definition.

01:05:25.530 --> 01:05:29.390 align:middle line:84%
Let's say that we call
H the sum of energy

01:05:29.390 --> 01:05:32.100 align:middle line:84%
plus the product of
pressure and volume.

01:05:32.100 --> 01:05:33.160 align:middle line:90%
We call it enthalpy.

01:05:33.160 --> 01:05:38.750 align:middle line:90%


01:05:38.750 --> 01:05:43.520 align:middle line:84%
Then by taking the
differential of this expression

01:05:43.520 --> 01:05:46.220 align:middle line:84%
and recalling that the
differential of a product

01:05:46.220 --> 01:05:54.950 align:middle line:84%
is equal to pdV plus
Vdp, where I see dE,

01:05:54.950 --> 01:06:00.080 align:middle line:84%
I use the differential that
I have written up here.

01:06:00.080 --> 01:06:01.370 align:middle line:90%
So I substitute.

01:06:01.370 --> 01:06:04.040 align:middle line:90%
And this is what I'm left with.

01:06:04.040 --> 01:06:06.950 align:middle line:90%
From this expression--

01:06:06.950 --> 01:06:13.570 align:middle line:84%
I can view this expression
as the differential.

01:06:13.570 --> 01:06:19.990 align:middle line:84%
So you see, the independent
variables are under the d--

01:06:19.990 --> 01:06:22.560 align:middle line:90%
so dS, dp, dn.

01:06:22.560 --> 01:06:27.190 align:middle line:90%


01:06:27.190 --> 01:06:29.020 align:middle line:84%
So this would be
the differential

01:06:29.020 --> 01:06:34.160 align:middle line:84%
of a function in which H is
a function of S, p, and n.

01:06:34.160 --> 01:06:38.440 align:middle line:90%


01:06:38.440 --> 01:06:42.100 align:middle line:84%
And also, the coefficients
of the differential

01:06:42.100 --> 01:06:43.780 align:middle line:90%
are the partial derivatives.

01:06:43.780 --> 01:06:47.230 align:middle line:84%
So for example, the
T is the partial

01:06:47.230 --> 01:06:51.820 align:middle line:84%
of H with respect to
S. The partial of what?

01:06:51.820 --> 01:06:55.200 align:middle line:84%
The partial of this
function, so the partial

01:06:55.200 --> 01:06:59.550 align:middle line:84%
of a function in which
the enthalpy is expressed

01:06:59.550 --> 01:07:03.780 align:middle line:90%
as a function of S, p, and n.

01:07:03.780 --> 01:07:06.460 align:middle line:90%
So that's the temperature.

01:07:06.460 --> 01:07:11.480 align:middle line:90%


01:07:11.480 --> 01:07:19.030 align:middle line:84%
Now, in the business of
measuring properties,

01:07:19.030 --> 01:07:21.460 align:middle line:90%
we like to have instruments.

01:07:21.460 --> 01:07:26.320 align:middle line:84%
So we have a thermometer
that measures temperature.

01:07:26.320 --> 01:07:30.610 align:middle line:84%
A manometer measures
the pressure.

01:07:30.610 --> 01:07:33.700 align:middle line:90%
There is no energy meter.

01:07:33.700 --> 01:07:37.090 align:middle line:90%
There is no entropy meter.

01:07:37.090 --> 01:07:40.330 align:middle line:84%
We measure energy and
entropy indirectly

01:07:40.330 --> 01:07:48.765 align:middle line:84%
through temperature and
pressure and volume.

01:07:48.765 --> 01:07:53.470 align:middle line:90%


01:07:53.470 --> 01:07:55.850 align:middle line:84%
So let's do that
also mathematically.

01:07:55.850 --> 01:07:59.620 align:middle line:84%
So you look at this equation
here and this other equation,

01:07:59.620 --> 01:08:04.450 align:middle line:84%
and consider it as a system of
two equations in which you want

01:08:04.450 --> 01:08:09.910 align:middle line:84%
to eliminate the property that
is hardly measurable-- difficult

01:08:09.910 --> 01:08:12.610 align:middle line:84%
to measure, hard to measure,
which is the entropy.

01:08:12.610 --> 01:08:21.010 align:middle line:84%
So for example, solve
this expression,

01:08:21.010 --> 01:08:23.410 align:middle line:84%
this function here as
a function-- instead

01:08:23.410 --> 01:08:27.130 align:middle line:84%
of T as a function of S, write
it as S as a function of T.

01:08:27.130 --> 01:08:32.450 align:middle line:84%
And then take that S and put
it in the original function

01:08:32.450 --> 01:08:34.029 align:middle line:90%
up there.

01:08:34.029 --> 01:08:39.060 align:middle line:84%
You manage to find H as
a function of T, p, n.

01:08:39.060 --> 01:08:41.830 align:middle line:84%
So you change the
independent variables

01:08:41.830 --> 01:08:45.790 align:middle line:84%
to ones that can
be easily measured,

01:08:45.790 --> 01:08:48.859 align:middle line:90%
temperature and pressure.

01:08:48.859 --> 01:08:52.189 align:middle line:84%
So this new function-- and this
is the way you have obtained

01:08:52.189 --> 01:08:54.020 align:middle line:90%
it-- so we have a precise way--

01:08:54.020 --> 01:08:57.080 align:middle line:84%
recipe to obtain that
function, if we start

01:08:57.080 --> 01:08:59.989 align:middle line:90%
from the fundamental relation--

01:08:59.989 --> 01:09:03.720 align:middle line:84%
is-- of this function,
you can take derivatives.

01:09:03.720 --> 01:09:07.250 align:middle line:84%
For example, the derivative
of H with respect to T

01:09:07.250 --> 01:09:10.069 align:middle line:84%
is what we call
the specific heat--

01:09:10.069 --> 01:09:14.250 align:middle line:84%
sorry, the heat capacity
at constant pressure.

01:09:14.250 --> 01:09:18.220 align:middle line:90%
And it is a function of T and p.

01:09:18.220 --> 01:09:21.520 align:middle line:84%
So pressure and
temperature, we can measure.

01:09:21.520 --> 01:09:26.649 align:middle line:84%
Heat capacity we can measure
with this instrument here.

01:09:26.649 --> 01:09:29.970 align:middle line:84%
And so this is a fully
measurable function.

01:09:29.970 --> 01:09:35.840 align:middle line:90%


01:09:35.840 --> 01:09:42.260 align:middle line:84%
A similar procedure we can
follow to define the heat

01:09:42.260 --> 01:09:45.950 align:middle line:90%
capacity at constant volume.

01:09:45.950 --> 01:09:48.535 align:middle line:84%
So we start again from
the fundamental relation.

01:09:48.535 --> 01:09:51.040 align:middle line:90%


01:09:51.040 --> 01:09:54.160 align:middle line:84%
And notice that the
temperature, which

01:09:54.160 --> 01:09:58.660 align:middle line:84%
is the partial derivative
of E with respect to S,

01:09:58.660 --> 01:10:02.020 align:middle line:84%
is being a function
of this variable--

01:10:02.020 --> 01:10:04.300 align:middle line:84%
I mean, a derivative of a
function of these variables

01:10:04.300 --> 01:10:06.440 align:middle line:84%
has the same
independent variables.

01:10:06.440 --> 01:10:09.460 align:middle line:84%
So it's also a function
of S, V, and n.

01:10:09.460 --> 01:10:13.210 align:middle line:84%
And also here, play
the game of eliminating

01:10:13.210 --> 01:10:20.350 align:middle line:84%
the not so easy to
measure property, entropy.

01:10:20.350 --> 01:10:28.530 align:middle line:84%
So solve this as S function
of T and substitute up there

01:10:28.530 --> 01:10:30.780 align:middle line:90%
to obtain that the energy--

01:10:30.780 --> 01:10:33.690 align:middle line:84%
a new function in
which the energy

01:10:33.690 --> 01:10:36.490 align:middle line:84%
is expressed in terms of
the independent variables,

01:10:36.490 --> 01:10:37.850 align:middle line:90%
temperature and volume.

01:10:37.850 --> 01:10:42.420 align:middle line:84%
These are things that are easy
to measure because temperature

01:10:42.420 --> 01:10:48.100 align:middle line:84%
you measure with the
thermometer, volume you

01:10:48.100 --> 01:10:51.330 align:middle line:90%
measure with the stick.

01:10:51.330 --> 01:10:54.010 align:middle line:90%


01:10:54.010 --> 01:10:56.950 align:middle line:84%
So the first derivative
of this function,

01:10:56.950 --> 01:10:59.200 align:middle line:84%
the partial of E
with respect to T,

01:10:59.200 --> 01:11:06.560 align:middle line:84%
is called the heat capacity
at constant volume.

01:11:06.560 --> 01:11:11.170 align:middle line:84%
And it is the thing that you
measure with that other Joule

01:11:11.170 --> 01:11:15.190 align:middle line:90%
apparatus at constant volume.

01:11:15.190 --> 01:11:16.340 align:middle line:90%
So we retain that.

01:11:16.340 --> 01:11:19.760 align:middle line:90%


01:11:19.760 --> 01:11:22.950 align:middle line:84%
But we can also do
this other procedure.

01:11:22.950 --> 01:11:26.190 align:middle line:84%
We take the temperature,
like before here,

01:11:26.190 --> 01:11:28.740 align:middle line:84%
but now we make a system
also with the pressure.

01:11:28.740 --> 01:11:33.530 align:middle line:84%
The pressure is the derivative
of E with respect to V.

01:11:33.530 --> 01:11:35.510 align:middle line:84%
And being a derivative
of a function

01:11:35.510 --> 01:11:37.170 align:middle line:84%
with these
independent variables,

01:11:37.170 --> 01:11:40.130 align:middle line:84%
it also has the same
independent variables.

01:11:40.130 --> 01:11:42.520 align:middle line:84%
Eliminate entropy
also from these two.

01:11:42.520 --> 01:11:45.230 align:middle line:90%


01:11:45.230 --> 01:11:50.130 align:middle line:84%
That results in a relation
between pressure, volume,

01:11:50.130 --> 01:11:53.930 align:middle line:84%
and temperature, which we
call the equation of state.

01:11:53.930 --> 01:11:55.760 align:middle line:84%
Pressure, volume,
and temperature

01:11:55.760 --> 01:11:59.510 align:middle line:84%
are also easily
measurable stuff.

01:11:59.510 --> 01:12:01.640 align:middle line:90%
That's the equation of state.

01:12:01.640 --> 01:12:08.270 align:middle line:84%
And the partial derivatives
of this equation of state--

01:12:08.270 --> 01:12:12.860 align:middle line:84%
so the derivative of
V with respect to T,

01:12:12.860 --> 01:12:18.510 align:middle line:84%
says how much the
volume of your substance

01:12:18.510 --> 01:12:23.450 align:middle line:84%
changes as you vary the
temperature, as you heat it up.

01:12:23.450 --> 01:12:27.550 align:middle line:84%
So it's the coefficient
of expansion.

01:12:27.550 --> 01:12:31.530 align:middle line:84%
If you do it divided by V,
it's the percentage increase

01:12:31.530 --> 01:12:33.870 align:middle line:90%
in volume per given amount--

01:12:33.870 --> 01:12:38.160 align:middle line:84%
or given increase
in temperature.

01:12:38.160 --> 01:12:44.190 align:middle line:84%
And you can measure this
when you do the experiment

01:12:44.190 --> 01:12:45.450 align:middle line:90%
at constant pressure.

01:12:45.450 --> 01:12:48.690 align:middle line:84%
Or the second, the
other derivative,

01:12:48.690 --> 01:12:53.190 align:middle line:84%
the derivative of V
with respect to P,

01:12:53.190 --> 01:13:02.430 align:middle line:84%
it says how much the substance
gets reduced in volume if I

01:13:02.430 --> 01:13:05.430 align:middle line:90%
increase the pressure.

01:13:05.430 --> 01:13:10.200 align:middle line:84%
So the reduction
is minus delta V

01:13:10.200 --> 01:13:12.670 align:middle line:84%
per unit of increase
in pressure.

01:13:12.670 --> 01:13:15.030 align:middle line:84%
And again, if I
divide by V, it's

01:13:15.030 --> 01:13:25.280 align:middle line:84%
the percentage
reduction in volume.

01:13:25.280 --> 01:13:30.080 align:middle line:84%
So when you do the experiment,
increase the pressure

01:13:30.080 --> 01:13:31.800 align:middle line:90%
at constant temperature.

01:13:31.800 --> 01:13:35.000 align:middle line:84%
This is the isothermal
compressibility

01:13:35.000 --> 01:13:37.750 align:middle line:90%
of the substance.

01:13:37.750 --> 01:13:39.950 align:middle line:84%
Being derivatives of
the equation of state,

01:13:39.950 --> 01:13:43.510 align:middle line:84%
they are functions of T
and P. And these are easily

01:13:43.510 --> 01:13:46.420 align:middle line:84%
measured because
it simply relates

01:13:46.420 --> 01:13:49.760 align:middle line:84%
measuring changes in volume,
measuring temperatures.

01:13:49.760 --> 01:13:54.570 align:middle line:90%


01:13:54.570 --> 01:13:57.210 align:middle line:84%
So the differential
of the equation

01:13:57.210 --> 01:14:08.660 align:middle line:84%
of state done at fixed amounts
has these two coefficients,

01:14:08.660 --> 01:14:11.510 align:middle line:84%
isobaric expansion and
isothermal compressibility

01:14:11.510 --> 01:14:14.200 align:middle line:90%
appearing directly here.

01:14:14.200 --> 01:14:17.100 align:middle line:90%


01:14:17.100 --> 01:14:18.990 align:middle line:84%
There are other
things that you can

01:14:18.990 --> 01:14:21.400 align:middle line:90%
measure in other experiments.

01:14:21.400 --> 01:14:25.470 align:middle line:84%
For example, an
interesting one is

01:14:25.470 --> 01:14:31.765 align:middle line:90%
the speed of sound propagation.

01:14:31.765 --> 01:14:33.800 align:middle line:90%
It should be an of here.

01:14:33.800 --> 01:14:40.370 align:middle line:84%
Or the Joule-Thomson
coefficient in the expansion

01:14:40.370 --> 01:14:45.440 align:middle line:84%
of a gas in a throttle, which
occurs at constant enthalpy.

01:14:45.440 --> 01:14:47.540 align:middle line:84%
You measure the
change in temperature

01:14:47.540 --> 01:14:50.720 align:middle line:90%
over a drop in pressure.

01:14:50.720 --> 01:14:53.030 align:middle line:84%
And it can be
positive and negative.

01:14:53.030 --> 01:15:00.770 align:middle line:84%
And that is related to
the things, the properties

01:15:00.770 --> 01:15:02.870 align:middle line:84%
that we have already
defined before.

01:15:02.870 --> 01:15:08.060 align:middle line:84%
And also, the Mayer
relation shows

01:15:08.060 --> 01:15:16.580 align:middle line:84%
that Cp, CV, alpha p, and
kappa T are not independent.

01:15:16.580 --> 01:15:19.770 align:middle line:84%
So you don't need to
measure all four of them.

01:15:19.770 --> 01:15:21.280 align:middle line:90%
You just need to measure three.

01:15:21.280 --> 01:15:34.270 align:middle line:90%


01:15:34.270 --> 01:15:37.640 align:middle line:84%
Let me skip that
one for a moment.

01:15:37.640 --> 01:15:39.260 align:middle line:90%
No, no, I need it.

01:15:39.260 --> 01:15:39.810 align:middle line:90%
I need it.

01:15:39.810 --> 01:15:42.850 align:middle line:84%
In order to measure
chemical potentials,

01:15:42.850 --> 01:15:46.780 align:middle line:84%
I do need first to show that
the chemical potentials can

01:15:46.780 --> 01:15:51.720 align:middle line:84%
be written as functions of
temperature and pressure.

01:15:51.720 --> 01:15:56.870 align:middle line:90%


01:15:56.870 --> 01:15:59.990 align:middle line:84%
Because you see, the
chemical potential

01:15:59.990 --> 01:16:02.870 align:middle line:84%
is defined as the
partial of E with respect

01:16:02.870 --> 01:16:09.200 align:middle line:84%
to n at constant S and
V, but that way, it

01:16:09.200 --> 01:16:13.430 align:middle line:84%
isn't easy to measure
because of the S.

01:16:13.430 --> 01:16:23.120 align:middle line:84%
So mu i is the partial of E with
respect to ni at constant S, V

01:16:23.120 --> 01:16:28.820 align:middle line:90%
and all the other n's held--

01:16:28.820 --> 01:16:32.660 align:middle line:84%
well, I shouldn't say that,
where the function that I am

01:16:32.660 --> 01:16:35.913 align:middle line:84%
taking the derivative of
is a function of S, V,

01:16:35.913 --> 01:16:36.580 align:middle line:90%
and all the n's.

01:16:36.580 --> 01:16:39.470 align:middle line:90%


01:16:39.470 --> 01:16:43.740 align:middle line:84%
However, when you
view it this way,

01:16:43.740 --> 01:16:49.130 align:middle line:84%
it's not easy to measure because
I don't have an energy meter

01:16:49.130 --> 01:16:50.635 align:middle line:84%
and I don't have
an entropy meter.

01:16:50.635 --> 01:16:53.820 align:middle line:90%


01:16:53.820 --> 01:16:58.120 align:middle line:84%
So the trick is to
change variables.

01:16:58.120 --> 01:17:01.720 align:middle line:84%
And one way to do it is to
define a function, which is

01:17:01.720 --> 01:17:07.510 align:middle line:90%
called the Gibbs free energy.

01:17:07.510 --> 01:17:10.970 align:middle line:84%
For the moment, think of it as
just an arbitrary definition.

01:17:10.970 --> 01:17:15.360 align:middle line:84%
So I say, define this
energy minus TS plus pV.

01:17:15.360 --> 01:17:18.430 align:middle line:90%


01:17:18.430 --> 01:17:20.650 align:middle line:90%
Write the differential.

01:17:20.650 --> 01:17:22.990 align:middle line:84%
Use the differential of
a fundamental relation

01:17:22.990 --> 01:17:25.030 align:middle line:90%
in order to express dE.

01:17:25.030 --> 01:17:28.510 align:middle line:84%
And here is what
you are left with.

01:17:28.510 --> 01:17:32.320 align:middle line:84%
This expression shows that
you can view this function

01:17:32.320 --> 01:17:36.670 align:middle line:84%
G as a function of the
independent variables that

01:17:36.670 --> 01:17:39.190 align:middle line:84%
appear under the d of
the differential-- so

01:17:39.190 --> 01:17:42.520 align:middle line:84%
the temperature, the
pressure, and the amounts.

01:17:42.520 --> 01:17:50.740 align:middle line:84%
So G has as, say, natural
variables, T, p and n.

01:17:50.740 --> 01:17:53.450 align:middle line:84%
And since this is the
differential of that function,

01:17:53.450 --> 01:17:57.670 align:middle line:84%
the chemical potential
can therefore

01:17:57.670 --> 01:18:04.440 align:middle line:84%
be written now also as the
partial of G with respect to ni.

01:18:04.440 --> 01:18:07.710 align:middle line:90%


01:18:07.710 --> 01:18:09.750 align:middle line:84%
And since it is a
partial of G, which

01:18:09.750 --> 01:18:11.700 align:middle line:84%
is a function of
T, p, and n, it's

01:18:11.700 --> 01:18:14.960 align:middle line:84%
also a function of
just T, p, and n.

01:18:14.960 --> 01:18:20.520 align:middle line:84%
So the chemical potential,
we would like to measure it.

01:18:20.520 --> 01:18:22.910 align:middle line:84%
It is very important to
determine the properties

01:18:22.910 --> 01:18:26.335 align:middle line:90%
of multi-component systems.

01:18:26.335 --> 01:18:29.620 align:middle line:90%


01:18:29.620 --> 01:18:31.850 align:middle line:84%
But it cannot be
measured directly.

01:18:31.850 --> 01:18:38.320 align:middle line:84%
There is no chemical
potential meter.

01:18:38.320 --> 01:18:41.770 align:middle line:84%
However, it can be
measured indirectly

01:18:41.770 --> 01:18:44.920 align:middle line:84%
via the definition of what
we call the partial pressure

01:18:44.920 --> 01:18:48.580 align:middle line:90%
of a component in the mixture.

01:18:48.580 --> 01:18:51.520 align:middle line:84%
Here, the experimental
setup is this.

01:18:51.520 --> 01:18:54.820 align:middle line:84%
I have my mixture in which
I have many components.

01:18:54.820 --> 01:18:58.360 align:middle line:84%
And they are in a stable
equilibrium state.

01:18:58.360 --> 01:19:01.610 align:middle line:84%
They are at some pressure,
some temperature,

01:19:01.610 --> 01:19:04.520 align:middle line:84%
and they have their chemical
potentials, and so on.

01:19:04.520 --> 01:19:07.120 align:middle line:90%


01:19:07.120 --> 01:19:12.340 align:middle line:84%
So what I do is to drill a
hole in the wall somewhere

01:19:12.340 --> 01:19:18.070 align:middle line:84%
of my system and
substitute the wall

01:19:18.070 --> 01:19:21.370 align:middle line:84%
with a membrane, a
semi-permeable or porous medium,

01:19:21.370 --> 01:19:26.320 align:middle line:84%
or a semi-permeable membrane,
where only molecules of type

01:19:26.320 --> 01:19:28.490 align:middle line:90%
I can cross.

01:19:28.490 --> 01:19:30.150 align:middle line:90%
The others don't.

01:19:30.150 --> 01:19:37.765 align:middle line:90%


01:19:37.765 --> 01:19:39.590 align:middle line:90%
So I put on the other side--

01:19:39.590 --> 01:19:47.765 align:middle line:84%
I put on the other side
molecules of substance i.

01:19:47.765 --> 01:19:50.410 align:middle line:84%
And with a piston,
I keep them there.

01:19:50.410 --> 01:19:52.390 align:middle line:84%
And I measure the
force per unit area

01:19:52.390 --> 01:20:01.040 align:middle line:84%
that is necessary to keep
them in mutual equilibrium.

01:20:01.040 --> 01:20:07.592 align:middle line:84%
When I reach mutual equilibrium
between this little system, ii,

01:20:07.592 --> 01:20:13.660 align:middle line:84%
the double script i
we use as a way to say

01:20:13.660 --> 01:20:15.470 align:middle line:90%
that it is a pure substance.

01:20:15.470 --> 01:20:23.770 align:middle line:84%
So in this little box,
there is only substance i,

01:20:23.770 --> 01:20:26.800 align:middle line:84%
whereas in the mixture
there is substance i mixed

01:20:26.800 --> 01:20:29.610 align:middle line:90%
with other stuff.

01:20:29.610 --> 01:20:32.430 align:middle line:84%
When we are in
mutual equilibrium

01:20:32.430 --> 01:20:37.740 align:middle line:84%
across this membrane,
we have proved also

01:20:37.740 --> 01:20:40.740 align:middle line:84%
the other day that
the conditions

01:20:40.740 --> 01:20:44.440 align:middle line:84%
for mutual equilibrium are
equality of temperature--

01:20:44.440 --> 01:20:47.400 align:middle line:90%


01:20:47.400 --> 01:20:49.590 align:middle line:84%
so the temperature
of system ii must

01:20:49.590 --> 01:20:52.440 align:middle line:84%
be equal to the
temperature of the mixture.

01:20:52.440 --> 01:20:56.610 align:middle line:84%
And the equality of chemical
potentials for the substance

01:20:56.610 --> 01:20:58.406 align:middle line:90%
that can be exchanged.

01:20:58.406 --> 01:21:01.620 align:middle line:90%


01:21:01.620 --> 01:21:03.870 align:middle line:90%
So the substance is i.

01:21:03.870 --> 01:21:06.000 align:middle line:84%
And so I need that
the chemical potential

01:21:06.000 --> 01:21:11.070 align:middle line:84%
of substance i of
the mixture must

01:21:11.070 --> 01:21:15.420 align:middle line:84%
be equal to the chemical
potential of the pure substance

01:21:15.420 --> 01:21:19.670 align:middle line:84%
i just on the other side of
a semi-permeable membrane.

01:21:19.670 --> 01:21:26.050 align:middle line:90%


01:21:26.050 --> 01:21:26.770 align:middle line:90%
OK.

01:21:26.770 --> 01:21:30.430 align:middle line:84%
Here, I also put the
functional dependence

01:21:30.430 --> 01:21:35.140 align:middle line:84%
because I used what we just
proved before, that the chemical

01:21:35.140 --> 01:21:38.230 align:middle line:90%
potential are functions--

01:21:38.230 --> 01:21:42.670 align:middle line:84%
can be written as
functions of T and p.

01:21:42.670 --> 01:21:45.160 align:middle line:84%
And so these are the
functions that we are going

01:21:45.160 --> 01:21:47.210 align:middle line:90%
to use for this measurement.

01:21:47.210 --> 01:21:52.500 align:middle line:90%


01:21:52.500 --> 01:21:59.460 align:middle line:84%
So by looking at
this equation, which

01:21:59.460 --> 01:22:06.840 align:middle line:84%
is required by the condition
for mutual equilibrium,

01:22:06.840 --> 01:22:13.140 align:middle line:84%
we see that inside the
independent variables are all

01:22:13.140 --> 01:22:17.680 align:middle line:90%
easily measurable things--

01:22:17.680 --> 01:22:24.700 align:middle line:84%
temperature, pressure,
and also this pii,

01:22:24.700 --> 01:22:29.260 align:middle line:84%
it's the pressure of the
system on the other side

01:22:29.260 --> 01:22:31.390 align:middle line:90%
of the semi-permeable membrane.

01:22:31.390 --> 01:22:34.330 align:middle line:84%
We call that pressure
the partial pressure

01:22:34.330 --> 01:22:36.700 align:middle line:90%
of constituent i in the mixture.

01:22:36.700 --> 01:22:39.550 align:middle line:90%
It is a property of the mixture.

01:22:39.550 --> 01:22:42.730 align:middle line:90%
And it can be measured.

01:22:42.730 --> 01:22:46.090 align:middle line:84%
And by measuring
it, and by knowing

01:22:46.090 --> 01:22:48.460 align:middle line:84%
how the chemical potential
of the pure substance

01:22:48.460 --> 01:22:52.490 align:middle line:84%
depends on-- so if I know
this for the pure substance,

01:22:52.490 --> 01:22:55.000 align:middle line:84%
I can infer from
that measurement

01:22:55.000 --> 01:22:59.030 align:middle line:84%
the chemical potential of the
constituent in the mixture.

01:22:59.030 --> 01:23:01.883 align:middle line:84%
This is how we
characterize mixtures.

01:23:01.883 --> 01:23:07.740 align:middle line:90%


01:23:07.740 --> 01:23:11.040 align:middle line:84%
So here is a little
summary of properties

01:23:11.040 --> 01:23:14.220 align:middle line:84%
that we have talked
about so far--

01:23:14.220 --> 01:23:20.290 align:middle line:84%
energy, entropy,
also the volumes

01:23:20.290 --> 01:23:23.011 align:middle line:84%
and the parameters
that enter in--

01:23:23.011 --> 01:23:26.020 align:middle line:84%
the amounts of constituents
that enter in the definition

01:23:26.020 --> 01:23:29.200 align:middle line:90%
of our system.

01:23:29.200 --> 01:23:33.970 align:middle line:84%
These properties are defined
for all states, equilibrium

01:23:33.970 --> 01:23:35.150 align:middle line:90%
and non-equilibrium.

01:23:35.150 --> 01:23:38.250 align:middle line:90%


01:23:38.250 --> 01:23:44.070 align:middle line:84%
Then we defined some
other properties

01:23:44.070 --> 01:23:47.070 align:middle line:84%
based on the fundamental
relation for stable equilibrium

01:23:47.070 --> 01:23:49.710 align:middle line:90%
states.

01:23:49.710 --> 01:23:51.990 align:middle line:84%
So clearly, these are
defined only if you

01:23:51.990 --> 01:23:54.450 align:middle line:90%
have a fundamental relation.

01:23:54.450 --> 01:23:58.230 align:middle line:84%
So they are defined only for
stable equilibrium states--

01:23:58.230 --> 01:24:02.280 align:middle line:84%
temperature, pressure, chemical
potentials, the enthalpy,

01:24:02.280 --> 01:24:11.370 align:middle line:84%
the Gibbs free energy, the
enthalpy because it's E plus pV

01:24:11.370 --> 01:24:13.030 align:middle line:90%
and p is the pressure.

01:24:13.030 --> 01:24:16.050 align:middle line:84%
Pressure is defined only
for a stable equilibrium.

01:24:16.050 --> 01:24:19.870 align:middle line:84%
Or the Gibbs free energy
has the p and the T also.

01:24:19.870 --> 01:24:24.710 align:middle line:84%
So it also is defined only
for stable equilibrium states.

01:24:24.710 --> 01:24:27.550 align:middle line:90%


01:24:27.550 --> 01:24:34.780 align:middle line:84%
And then we also defined
these four properties today--

01:24:34.780 --> 01:24:41.290 align:middle line:84%
the heat capacities, the
coefficient of expansion,

01:24:41.290 --> 01:24:45.640 align:middle line:84%
and the coefficient
of compressibility.

01:24:45.640 --> 01:24:51.880 align:middle line:84%
These ones also are restricted
for equilibrium states.

01:24:51.880 --> 01:24:54.520 align:middle line:84%
But they're even more
restricted because some

01:24:54.520 --> 01:24:57.525 align:middle line:84%
of those mathematical
steps that--

01:24:57.525 --> 01:25:00.190 align:middle line:90%


01:25:00.190 --> 01:25:07.060 align:middle line:84%
for example, if I
go back here, when

01:25:07.060 --> 01:25:11.080 align:middle line:84%
I do this eliminating
one variable,

01:25:11.080 --> 01:25:19.340 align:middle line:84%
I can do that only if some
derivative is not equal to 0.

01:25:19.340 --> 01:25:30.270 align:middle line:84%
So for example, if the partial
of T with respect to S is equal

01:25:30.270 --> 01:25:37.080 align:middle line:84%
to 0, I cannot invert that
function because it's not

01:25:37.080 --> 01:25:39.210 align:middle line:90%
monotonic.

01:25:39.210 --> 01:25:44.440 align:middle line:84%
And this is what
happens, for example,

01:25:44.440 --> 01:25:50.400 align:middle line:84%
when I have two-phase
states, like liquid and vapor

01:25:50.400 --> 01:25:52.380 align:middle line:90%
coexisting.

01:25:52.380 --> 01:25:58.470 align:middle line:84%
In that case, some
of these functions

01:25:58.470 --> 01:26:06.365 align:middle line:84%
are not defined or, which is the
same, take up infinite values.

01:26:06.365 --> 01:26:10.600 align:middle line:90%


01:26:10.600 --> 01:26:13.485 align:middle line:90%
So we go back to here.

01:26:13.485 --> 01:26:16.430 align:middle line:90%


01:26:16.430 --> 01:26:29.180 align:middle line:84%
Now, this also says that
if we do our measurements

01:26:29.180 --> 01:26:32.030 align:middle line:84%
and we can, for a
given substance,

01:26:32.030 --> 01:26:38.030 align:middle line:84%
or for a set of mixtures,
develop or measure

01:26:38.030 --> 01:26:42.020 align:middle line:84%
experimentally these
functions, the alpha p

01:26:42.020 --> 01:26:45.500 align:middle line:84%
as a function of T, p,
and composition, kappa T,

01:26:45.500 --> 01:26:48.260 align:middle line:84%
is a function of temperature,
pressure and composition.

01:26:48.260 --> 01:26:49.820 align:middle line:90%
The specific heat at constant--

01:26:49.820 --> 01:26:52.268 align:middle line:84%
I'm sorry, the heat capacity
at constant pressure

01:26:52.268 --> 01:26:54.560 align:middle line:84%
as a function of temperature,
pressure, and composition

01:26:54.560 --> 01:26:57.870 align:middle line:84%
and the chemical potentials
as a function of temperature,

01:26:57.870 --> 01:26:59.100 align:middle line:90%
pressure, and composition.

01:26:59.100 --> 01:27:05.690 align:middle line:84%
If I have all these functions,
then, with these functions,

01:27:05.690 --> 01:27:09.900 align:middle line:84%
I can reconstruct the
fundamental relation.

01:27:09.900 --> 01:27:11.720 align:middle line:84%
So I know everything
that I need to know

01:27:11.720 --> 01:27:15.800 align:middle line:84%
about the stable equilibrium
states of that substance.

01:27:15.800 --> 01:27:21.750 align:middle line:84%
And actually, the reconstruction
is done through these relations

01:27:21.750 --> 01:27:23.260 align:middle line:90%
here, for example, the energy.

01:27:23.260 --> 01:27:27.150 align:middle line:90%


01:27:27.150 --> 01:27:30.780 align:middle line:84%
These expressions
for the energy here

01:27:30.780 --> 01:27:36.030 align:middle line:84%
can be related to these
properties in this way.

01:27:36.030 --> 01:27:41.400 align:middle line:84%
So if I integrate from one
temperature to another,

01:27:41.400 --> 01:27:45.450 align:middle line:84%
from one pressure to
another, this expression,

01:27:45.450 --> 01:27:49.980 align:middle line:90%
I can get variations in energy.

01:27:49.980 --> 01:27:53.010 align:middle line:84%
The entropy also is
related this way.

01:27:53.010 --> 01:27:56.010 align:middle line:84%
The enthalpy is
related that way.

01:27:56.010 --> 01:28:00.510 align:middle line:84%
And these are general
forms that are

01:28:00.510 --> 01:28:03.630 align:middle line:90%
valid for any pure substance.

01:28:03.630 --> 01:28:09.700 align:middle line:84%
If you also need to
consider mixtures,

01:28:09.700 --> 01:28:14.670 align:middle line:84%
then you need to generalize this
to use the expressions where

01:28:14.670 --> 01:28:17.593 align:middle line:90%
also dn appears.

01:28:17.593 --> 01:28:20.390 align:middle line:90%


01:28:20.390 --> 01:28:32.770 align:middle line:84%
So in this way, we have a way to
measure the fundamental relation

01:28:32.770 --> 01:28:33.876 align:middle line:90%
of substances.

01:28:33.876 --> 01:28:36.610 align:middle line:90%


01:28:36.610 --> 01:28:37.110 align:middle line:90%
OK.

01:28:37.110 --> 01:28:42.078 align:middle line:90%


01:28:42.078 --> 01:28:46.045 align:middle line:90%
Now, yeah.

01:28:46.045 --> 01:28:47.170 align:middle line:90%
Yeah, we have five minutes.

01:28:47.170 --> 01:28:49.320 align:middle line:90%
I can do this.

01:28:49.320 --> 01:28:56.370 align:middle line:84%
I want to show that
some of these function,

01:28:56.370 --> 01:29:03.420 align:middle line:84%
like the enthalpy and
the Gibbs free energy,

01:29:03.420 --> 01:29:08.790 align:middle line:84%
are obtained as
Legendre transforms

01:29:08.790 --> 01:29:10.780 align:middle line:90%
of the fundamental relation.

01:29:10.780 --> 01:29:14.340 align:middle line:84%
Legendre transform is
a particular procedure

01:29:14.340 --> 01:29:19.980 align:middle line:90%
that we can explain in this way.

01:29:19.980 --> 01:29:24.570 align:middle line:84%
Let's start with the function
of a single variable.

01:29:24.570 --> 01:29:27.990 align:middle line:84%
So suppose you give me a
function of a single variable,

01:29:27.990 --> 01:29:32.310 align:middle line:90%
like any function.

01:29:32.310 --> 01:29:41.970 align:middle line:84%
But to simplify, let me suppose
that this function is either

01:29:41.970 --> 01:29:50.550 align:middle line:84%
convex or concave and monotonic
so that I can invert and play

01:29:50.550 --> 01:29:51.900 align:middle line:90%
with it.

01:29:51.900 --> 01:29:54.700 align:middle line:84%
So usually, we
define a function--

01:29:54.700 --> 01:30:05.040 align:middle line:84%
I'll call it f of y, meaning
that, for each value of y,

01:30:05.040 --> 01:30:06.305 align:middle line:90%
I get a value of f.

01:30:06.305 --> 01:30:09.360 align:middle line:90%


01:30:09.360 --> 01:30:15.810 align:middle line:84%
And as I move y, the function
tells me how f moves.

01:30:15.810 --> 01:30:17.700 align:middle line:90%
But there is an alternative.

01:30:17.700 --> 01:30:21.780 align:middle line:84%
The idea of Legendre
is that there

01:30:21.780 --> 01:30:26.940 align:middle line:84%
is an alternative description
because that function also has

01:30:26.940 --> 01:30:32.525 align:middle line:84%
a tangent and has a line
tangent to every point.

01:30:32.525 --> 01:30:35.910 align:middle line:90%


01:30:35.910 --> 01:30:44.130 align:middle line:84%
So this tangent is
characterized by two items, one

01:30:44.130 --> 01:30:51.630 align:middle line:84%
that we will call lambda, which
is the angular coefficient

01:30:51.630 --> 01:30:54.870 align:middle line:90%
or the slope of the line.

01:30:54.870 --> 01:31:00.420 align:middle line:84%
And this other value here,
that we call L, which

01:31:00.420 --> 01:31:04.460 align:middle line:90%
is the intercept at y equals 0.

01:31:04.460 --> 01:31:11.750 align:middle line:90%


01:31:11.750 --> 01:31:18.630 align:middle line:84%
So the idea of Legendre
is that you can--

01:31:18.630 --> 01:31:23.370 align:middle line:84%
if you draw, like
it's sketched here,

01:31:23.370 --> 01:31:25.840 align:middle line:84%
the slopes at every
point of the line,

01:31:25.840 --> 01:31:31.080 align:middle line:84%
you get a family of lines,
the envelope of which

01:31:31.080 --> 01:31:32.510 align:middle line:90%
is your original curve.

01:31:32.510 --> 01:31:37.160 align:middle line:90%


01:31:37.160 --> 01:31:44.750 align:middle line:84%
Each line is characterized for a
given lambda, for a given lambda

01:31:44.750 --> 01:31:49.840 align:middle line:90%
by L. I change the point.

01:31:49.840 --> 01:31:51.760 align:middle line:90%
So I take another lambda.

01:31:51.760 --> 01:31:56.370 align:middle line:84%
Suppose I want this
slope, this match.

01:31:56.370 --> 01:31:58.370 align:middle line:90%
So I fix lambda.

01:31:58.370 --> 01:32:01.310 align:middle line:90%
So say this is lambda 1.

01:32:01.310 --> 01:32:02.885 align:middle line:90%
Now, I fix lambda 2.

01:32:02.885 --> 01:32:05.900 align:middle line:90%


01:32:05.900 --> 01:32:11.930 align:middle line:90%
And that gives me L of 2.

01:32:11.930 --> 01:32:21.110 align:middle line:84%
So selecting a value
of lambda specifies,

01:32:21.110 --> 01:32:25.340 align:middle line:84%
selects the point
in which the tangent

01:32:25.340 --> 01:32:28.910 align:middle line:84%
as that slope, of
the original curve.

01:32:28.910 --> 01:32:33.860 align:middle line:84%
And therefore, when you
place your line there,

01:32:33.860 --> 01:32:38.400 align:middle line:90%
it also selects an intercept.

01:32:38.400 --> 01:32:44.280 align:middle line:84%
So there is a relation
between lambda and L.

01:32:44.280 --> 01:32:47.430 align:middle line:84%
And that relation is
the Legendre transform

01:32:47.430 --> 01:32:48.305 align:middle line:90%
of your function.

01:32:48.305 --> 01:32:52.780 align:middle line:90%


01:32:52.780 --> 01:33:01.150 align:middle line:84%
The procedure runs this way,
that you take the function,

01:33:01.150 --> 01:33:08.380 align:middle line:84%
you write the equation for the
partial, for the derivative.

01:33:08.380 --> 01:33:16.280 align:middle line:84%
And then you define L by the
geometrical construction.

01:33:16.280 --> 01:33:24.760 align:middle line:84%
So it's the function f
minus this distance here.

01:33:24.760 --> 01:33:35.680 align:middle line:84%
And this distance here is
equal to the horizontal segment

01:33:35.680 --> 01:33:41.050 align:middle line:84%
times the slope, so the tangent
of this angle, so lambda.

01:33:41.050 --> 01:33:48.705 align:middle line:84%
So L is equal to f
minus lambda times y.

01:33:48.705 --> 01:33:52.780 align:middle line:90%


01:33:52.780 --> 01:33:56.320 align:middle line:84%
So it corresponds
to that description.

01:33:56.320 --> 01:33:59.960 align:middle line:84%
And I think the time
is up for today.

01:33:59.960 --> 01:34:07.110 align:middle line:84%
So we'll pick it up
from here the next time.

01:34:07.110 --> 01:34:11.000 align:middle line:90%