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Lecture 19

Thermodynamics

The material in this chapter will probably leave you with a sense of dissatisfaction, since you wil be asked to believe several statements without any convincing proof. Still, these principles have extremely far reaching consequences for the technological world of today, and it is importnat to have some grasp of them (and it is also true that many of the concepts, athough their rigorous proof is beyond the scope of this course, are intuitive to a fair extent). I will also skip some of the details included in the textbook, while concentrating on the applications.

What we are going to study are the general relations that control the transformation (and the exploitation) of thermal energy into mechanical work. To do so we will consider thermodynamical systems, i.e. any suitable choice of objects, machinery (or possibly just a part of a machinery), etc. that interacts with its surroundings by exchanging energy in either direction (by surroundings we mean everything else in the universe, except for the components of the system). More specifically: In the past, we have often encountered the principle of Conservation of Mechanical Energy and have seen that to change the energy of a system some net work must be at play. Next, we have also learnt how there is a type of energy, thermal energy, that is associated with heat, and in fact a heat transfer represents a transfer of energy between two systems (or two components of a system). It is then rather immediate to express the principle of Energy Conservation when applied to thermodynamical systems : we will say that, in any thermodynamical process there must be a balance between heat exchanged, work done and change in internal energy, i.e.
Q = W + $\Delta U$
The most obvious situation is the one where both Q and W are positive : if I have some gas in the movable piston container, and heat it up, in general both work will be done (the gas will expand) and the internal energy (as measured by the gas temperature) will increase. But the expression, as it represents energy conservation, is equally valid for any possible sign choice of the three terms.

Examples : Problems 15.1, 15.3
The expression above, which is more often written as
$\Delta U$ = Q - W
represents the First Law of Thermodynamics. A simple way of expressing it is that you can't get more work than the amount of heat you put in (unless you deplete the internal energy of the system, which is of course finite) : there is no perpetual motion.

Thermal Processes, special cases

When studying the ideal gas law, we had already considerd the special cases of processes occurring respectively at constant pressure, constant volume or constant temperature (they go under the respective names of isobaric, isochoric and isothermal). Another important (ideal) case is when a thermodynamical system does not exchange any heat with the surroundings; this process is called adiabatic. What does the First Law tell us for these cases? The expression we have found for the work in the isobaric case can be extended to more general cases. The result W = P x $\Delta V$ can be interpreted by saying that work is given by the area enclosed in the Pressure vs. Volume graph. For the general case of non-constant pressure, we could still think of subdividing the whole process into many smal steps, such that in each step the pressure is almost constant, and for each of these steps the elementary work will be given by the product P x $\Delta V$. The total work wil be the sum of the small pieces, therefore again it will be given by the area under the P vs. V graph.

Section 15.5 : read and understand the concepts, but ignore formulae 15.3 and 15.5

Section 15.6 : skip


Heat Engines and the Second Law

It would be the subject for an interesting socio-historical study (and maybe someone has done it already) to understand why, even though the potential of heat (e.g. high pressure steam) to generate mechanical work was known since antiquity, practical applications did not occur until the 18th century, culminating with the achievements of the industrial revolution. Whatever the reason, it is a fact that the development of the heat engine occurred simultaneously with the formal development of the corresponding science branch, ie. Thermodynamics, and the two proceeded hand in hand, one advance in one prompting the next step in the other, as it is often the case in science.

But what is a heat engine? In its first instances, it is a device that converts thermal energy into mechanical work (today, we might also want to include among heat engines devices like air conditioners and refrigerators that perform a different task, i.e. they use energy to move heat "the wrong way"). But, as soon as you think of any traditional heat engine (steam locomotive, gasoline burning car, oil burning power station, etc.) you soon realize that, in any such applications, not all the thermal energy available at the input is transformed into mechanical work, but some of it remains in the form of thermal energy (either e.g. as heat generated by friction or by heat carried away by the exhaust system). Another apparently trivial consideration (but maybe not as trivial as it might appear) is that the work-producing heat source has to be at a higher temperature than the heat exhaust. In other words heat does not flow spontaneously from a colder to a hotter system (this is one of several equivalent ways of expressing the second Law of Thermodynamics.

But let's go back to our heat engine, and let's assume that it works in some sort of cyclical way : some amount of heat is given to the engine, which then produces a certain amount of work, it exhausts a certain amount of heat to the outside, and then gets ready to start another cycle by going back to the initial high temperature. In a full cycle there is no change in internal energy, therefore

W = Qin - Qout = QH - QC
where we use the indices H(ot) and C(old) to remember the temperature difference between the input and output heat. If we define as efficiency e of our engine the ratio of work output to energy (i.e. heat) input, we have
e = W/QH = (QH-QC)/QH = 1-QC/QH < 1
In general, it is not straightforward to estimate how much heat a given engine loses to its surroundings ( friction processes and the like are very hard to quantify), but theoretical studies of cyclical processes allowed to identify an ideal case representing the best possible theoretical performance a heat engine could ever achieve. The French scientist-engineer Sadi Carnot investigated the properties of reversible processes, i.e cyclical processes such that, at the end of the cycle, both the system and its environment return exactly at the original state (a perfectly reversible process is just an abstract concept, since it would require that every molecule gets back to its original position and velocity; it is as if, in an eight-ball pool game, the balls come back to their original position after the breaking).

Anyway the result of this study (i.e. the performance of a Carnot Cycle consisting of the sequence [isothermal (at temperature TH)-adiabatic-isothermal (at TC)-adiabatic] showed that the quantity 1-QC/QH represents in fact that upper limit of efficiency that a perfect machine could achieve. Moreover, it was shown that QC/QH = TC/TH, where TH and TC are respectively the absolute temperatures of the (hot) heat source and the (colder) heat sink. Consequently, the ultimate limit of efficiency for any possible heat engine is given by

e = 1-TC/TH < 1
This is a remarkable result, since it is independent of the type of machine, the source of thermal energy (steam, gasoline, etc.) and the process employed to produce work. It also says that the highest efficiency are achieved for the highest temperature differentials between heat source and sink, with e = 1 only approched in the (unrealistic and impractical) case T = absolute zero (although this is not too far from what is encounterd in outer space). From these results follows an alternative way of stating the Second Law of Thermodynamics: it is impossible to have a system whose sole result is the complete transformation of heat into an equivalent amount of mechanical work (notice that energy conservation , i.e. the first law , does allow in principle the processes that are forbidden by the second law). Perpetual motion is even harder than the first law might have implied !!

Refigerators, air conditioners, etc.

The second law of Thermodynamics tells you that heat does not travel spontaneously from a colder environment to a warmer one. But the law does not prevent you from achieving the "wrong direction" heat transfer by doing some work onto the system. And this is in fact what is done for refrigerators, air conditioners and heat pumps : in all of these cases, some amount of energy (typically electric energy, even though it would be possible in principle to run e.g. a refrigerator with a diesel engine or even with manual labour..) is used to do the work of transferring heat from a colder to a warmer environment (and as a consequence, the cold section becomes colder and the warm warmer). In the three common applications the cold and warm parts of the system are respectively:


Device Cold Reservoir Hot Reservoir
Fridge fridge insides kitchen
Air Conditioner room outdoors
Heat Pump outdoors inside of house
In all of these cases, the first law of thermodynamics, W = QH-QC, is still valid, but in each case QH and QC will have different meanings. Also for these devices, the performance is normally quoted in terms of a coefficient of performance rather than in terms of efficiency. How is this defined?

For a heat pump, the relevant quantity is the amount of heat brought into the house for a given amount of work, i.e.
coeff. of perf. = QH/W
Notice that this is just the inverse of the previously defined efficiency (=W/QH). But notice also that, for a heat pump, we would like "low efficiency", i.e large coefficent of performance. For a perfect (i.e. Carnot-like) device we also have :
QH/W = QH/(QH-QC) = ...... = TH/(TH-TC) > 1
which shows that the performance does depend on the two temperatures. Moreover, heat pumps do not perform very well when the outside temperature is too low.

For air conditioners and refrigerators, the relevant performance figure is how much heat can be removed from the cold reservoir for a given amount of work :
coeff. of perf. = QC/W
And, in a similar way we could see that the ideal performance is given by
QC/W = QC/(QH-QC) = ...... = TC/(TH-TC) > 1


Section 15.11, Entropy : skip

 
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Sergio Conetti
12/3/1999