Fig. 1
A p/v-diagram shows three isotherms and two adiabatics intersecting them. The intersection points are A, B, C, D; C is out of the diagram. A Carnot process may cycle through these four points. The dashed area is the work released by the process during one cycle.
Why cyclic? Well, if it isn't then the process causes additional changes in the surroundings. Look at these processes:
None of these processes can be reversed at the same conditions; the changes they cause are permanent. However, a heat engine should not cause permanent changes; all permanent changes of the process of converting heat into work are ascribed to the heat flow from the source to the sink, which are not part of the engine. Thus the process in the engine itself must be cyclic. This also helps in using the engine over and over <g>
= -w/q,
where -w
is the work the engine outputs (this is why it is negative), and q
q is the heat input. Thus we have
w = W1 + W2 + W3 + W4
q = Qhi + Qlo
Qhi > 0
at high temperature and outputs the heat
Qlo < 0
at low temperature. In the two expansion phases it outputs work into its surroundings
W1 < 0; W2 < 0
and in the compression phases work is done upon the engine
W3 > 0; W4 > 0
Total energy must be conserved (just another empirical law <g>) so
dU = 0 = q + w
It follows that
q = -w
and
Qhi + Qlo = -w
By definition
= -w/q = (Qhi + Qlo)/Qhi
(eqn. 1)
This is the maximum possible efficiency of a heat engine; if there was a more efficient heat engine, say one based on a different working substance, then one could build an engine that does nothing but convert heat into work and that is (empirically!) impossible. It follows that the formula gives the maximum efficiency independend of the working substance.
The efficiency of a Carnot cycle is a funcion of the two working temperatures (hi, lo are empirical temperatures) of the hot and cold heat reservoirs alone
= g (hi, lo)
(and we know that
g (hi, lo) = Qhi/Qlo
)
hence Qhi/Qlo
must also be a funcion of the two temperatures alone
Qhi/Qlo = f(hi, lo),
since
(Qhi + Qlo)/Qhi = 1 + Qhi/Qlo = g = f + 1
Consider two Carnot cycles on top of each other (see fig 1), sharing an isotherm at
2
,
where the first process cycles between
hi
and
2
(with heats involved Qhi
and Q2
, respectively) and the second at
2, lo
(heats Q2, Qlo
).
2
is between (hi, lo
).
Of course you can look at these processes as being one single process between
(hi,
lo
)
with heats involved (Qhi, Qlo
). Then
Qhi/Q2 = f
(hi,
2)
Q2/Qlo = f
(2,
lo)
Qhi/Qlo = f
(hi, lo)
By multiplying the first equation with the second you get the third, hence
f
(hi,
2)
* f(2,
lo)
= f(hi,
lo)
It is easy to see that this holds if
f(hi,
lo) = F(hi)
/ F(lo)
(and respectively for the other f's) where F denotes an arbitrary function of one variable (substitute the ratio of the capital F's for each f(hi, lo) and you will see!). It is probably much less easy to show that this is the only choice, but let us leave this to the mathematicians and trust them when they assert it is so. It follows that
Qhi/Qlo
= F(hi)
/F(lo)
It was Kelvin who used this equation to define a thermodynamic temperature, independend af any specific thermometric substance. Of course he put it the simplest way by defining F() = T
. From this follows
Qhi/Qlo = Thi/Tlo
or Qhi/Thi = Qlo/Tlo
or Q/T = constant
for a reversible Carnot process. The effectivity (eqn. 1) thus becomes
= 1 - Tlo/Thi
(eqn. 2)
If the working substance in the cylinder is an ideal gas, which is mathematically defined by
pV = nRT,
,
pressure times volume equals (number of moles) times (universal gas constant) times temperature
For a isothermal expansion of an ideal gas we have:
dW = pdV = RTdV/V = dQ,
(eqn. 3)
the latter equality being valid because for an isothermal expansion of an ideal gas dU = 0
. On integration
Q = RT ln (V2/V1)
Thus we have, respectively:
Qhi = RThi ln (VB/VA)
Qlo = RTlo ln (VD/VC)
(please refer to fig 1. for the identifiers). Put this into equation 1 to get:
Tlo * ln (VD/VC)
= __________________ + 1
Thi * ln (VB/VA)
It can be shown that
VB/VA = VD/VC
so that:
= 1 - Tlo/Thi
This is the same result as in equation 2, hence the two temperatures must be identical.