1. Introduction
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“The motive power of heat is independent of the agents employed to realize it; its quantity is fired solely by the temperatures of the bodies between which is effected, finally, the transfer of the caloric.”—by Sadi Carnot, 1824
(English Translation by Robert H. Thurston [
1]).
In 2024, the thermodynamic community celebrated
Sadi Carnot’s Legacy and the
200th Anniversary of his only and famous ‘
Réflexions’ publications, which was not appreciated at his time, and may only be truly comprehended by a few, even nowadays [
1,
2,
3,
4,
5]. It should be noted that original and ingenious Sady Carnot’s discoveries were expounded and formalized decades later by Kelvin [
6] and mostly by Clausius [
7], while some persistent post-misconceptions and fallacies by others are also presented here as ‘
Miss Points’. Even the ‘
Carnot Cycle efficiency’ per se is fundamentally misplaced as reasoned below.
Here, we present this author’s contribution with ‘2024
Key Reflections’ and the plenary presentation of his lifelong work at
Sadi Carnot’s Legacy International Colloquium at École Polytechnique in France [
3,
8].
As Anthony Legget, a Nobel laureate, commented, “Mathematical convenience versus physical insight […] that theorists are far too fond of fancy formalisms which are mathematically streamlined but whose connection with physics is at best at several removes […] heartfully agreed with Philippe Nozieres that ‘only simple qualitative arguments can reveal the fundamental physics’”. In that regard, instead of an extensive review of literature or an ‘extravagant’ historical or philosophical formal methodology (as performed by many), here, mostly thermodynamic, specific, and simple reasoning, but with deep intuitive comprehension, were emphasized by a lifelong engineering thermodynamicist, for the first time as such in the literature.
It is well known that “Thermodynamics is not easy to understand ‘the first time around’”. Thermodynamics is confusing until it is comprehended, and this work is no exception. Sometimes, interpretation by different experts may result in further confusion. Namely, not all scientists/physicists and engineers are thermodynamicists, and a “thermodynamic historian” is not a “thermodynamicist”, but a “historian”, often with elegant style and abstract methods, but sometimes without due comprehension of tacit thermodynamic fundamentals. We are often trapped in our own thoughts and words (especially in emerging new concepts and if non-native) and subtle holistic meanings are to be read “between the lines”. Sometimes, highly accomplished scientists in their fields do not fully comprehend the essence of thermodynamics, especially if related to the Second Law and entropy.
The objective of this article is not to formally review Carnot’s ‘
Réflexions’, nor the vast amount of related literature by others (which was already, in part, carried out by this author [
9,
10,
11] and many others, for example [
12,
13,
14,
15,
16]), but to present this author’s long-contemplated reflections, with critical thermodynamic insights and logical reasonings, and to put “key thermodynamic concepts” into a contemporary perspective. Namely, selective, physical, and sequential ‘
Key Points’, as judged by this author, where the ingenious Sadi Carnot’s reasoning infers the next one, along with ‘
Miss Points’, presenting persistent post-misconceptions and fallacies by others (that needed to be underscored and ‘
put to rest’), are presented as such for the first time. The emphasis is on engineering and phenomenological thermodynamics (on fundamental substance instead of formal methodology and style), and not on a philosophical and historical review and ‘extension’ of Carnot’s work (already carried out by many). Therefore, only selected and related publications by this author are referenced.
Sadi Carnot, at age 28 in 1824, published the now famous “
Réflexions sur la puissance motrice du feu” (English translation, “
Reflections on the Motive Power of Fire [
1]”). His ingenious reasoning of reversible processes and cycles, and maximum “
heat-to-power efficiency” laid the foundations for the
Second Law of thermodynamics, before
The First Law of energy conservation was even formulated (in the 1840s), and long before thermodynamic concepts were established [
6,
7] (in the 1850s and later elsewhere). Sadi Carnot, who died in 1832 at age 36 during a cholera epidemic, could not had been aware of the immense implications of his ingenious reasoning at that time. No wonder Sadi Carnot’s masterpiece, regardless of its flawed assumption of
conservation of caloric, was not appreciated at his time, when his ingenious reasoning of ideal “
heat engine reversible cycles” was not fully recognized; it may only be truly comprehended by a few, even nowadays.
Before this author’s “
2024 ‘Key Reflections’ on the 1824 Sadi Carnot’s ‘Réflexions’” are presented here, a brief introduction, based on his prior publications [
9,
10,
11], is given next to revisit the essential concepts. Note that Carnot’s
Réflexions focused on ideal, reversible cycles and maximum possible efficiency, hence the reversible processes and cycles are assumed here, unless specifically stated otherwise (as dissipative or irreversible). Furthermore, the concepts of
heat and
work were not well formalized in Carnot’s time, but
caloric and
motive power were used instead; the latter, as work rate or in short ‘
work’, is often used here (e.g., heat or work for duration of a cycle or for some time period, should be self-evident).
Sadi Carnot gave a full and accurate reasoning of heat engine cyclic processes and their limitations of “converting heat to [work] motive-power” at a time when caloric theory was flourishing and almost two decades before equivalency between work and heat was experimentally established by Joule and others, in the 1840s (see elsewhere).
At that time, when the energy conservation law was not known, heat was considered an indestructible caloric, and heat engines were in their initial stage of development with an efficiency of less than 5%, confusion and speculations flourished. Can efficiency be improved by different temperatures or pressures, a different working substance than water, or some different mode of operation other than pistons and cylinders? With ingenious and far-reaching reasoning, Sadi Carnot answered all of those questions and logically reasoned (thus proved) that the maximum, limiting efficiency of heat engines does not depend on the medium used in the engine or its design, but only depends on (and increases with) the temperature difference between the heat source and cooling medium or heat sink (however, not linearly), similarly to the waterwheel work–power dependence on the waterfall height difference at a given water flow rate, see Equation (1) and
Figure 1 (explicit formulas were developed after Carnot’s followers’ work [
6,
7] and elsewhere; see also
Miss Point 1 and
Key NOVEL-Point 4).
Most importantly, Carnot introduced reversible processes and cycles and, with the ingenious reasoning of “
Contradiction impossibility”, see
Key NOVEL-Point 3, proved that the maximum heat engine efficiency is achieved by any reversible cycle, thus, all must have the same maximum possible efficiency ([
1,
9,
10], see also
Key NOVEL-Point 2), i.e.,
“
The motive power of heat is independent of the agents employed to realize it; its quantity is fired solely by the temperatures of the bodies between which is effected, finally, the transfer of the caloric” [
1]. Namely,
The Carnot cycle consists of four reversible processes (see
Figure 2): isothermal heating and expansion at a constant
high temperature
TH (also referring to ‘
hot reservoir’ elsewhere;
process 1–2); adiabatic expansion to achieve a
low temperature
TL (also
TL ≡
TC referring to ‘
cold reservoir’ elsewhere;
process 2–3); isothermal cooling and compression at a constant low temperature
TL (
process 3–4); and adiabatic compression to achieve a high temperature
TH and complete the cycle (
process 4–1).
All processes are reversible; thus, the cycle could be reversed, without additional external intervention, along the same path and with the same quantities of all the heats and works in opposite directions (
in-to-out and vice versa), see Equation (2) and
Figure 3, i.e.:
The concept and consequences of a process and cycle reversibility are the most ingenious and far-reaching, see [
5,
9,
10] (see also
Key NOVEL-Point 1). Sadi Carnot’s simple and logical reasoning that mechanical work is extracted in a heat engine due to the heat passing from a high to low temperature (see also
Key Point I) led him to a very logical conclusion that any heat transfer from a high to low temperature (like in a heat exchanger) without extracting the possible work (like in a reversible heat engine) will be a waste of work potential, so he deduced that any heat transfer in an ideal, perfect heat engine must be at an infinitesimally small temperature difference (no loss of caloric fall potential), achieved via mechanical compression or the expansion of the working medium (required temperature adjustment without heat transfer), as Carnot ingeniously advised in full details [
1] (see also
Key Point II).
Then, Sadi Carnot expended his logical reasoning to conclude that all reversible (ideal) heat engines must have an equal and maximum possible efficiency, otherwise, if reversed, the impossible “
creation of conserved quantities” would be achieved, see all details in [
1,
9,
10] and elsewhere (see also
Key Point V and
Key NOVEL-Point 2). What ‘a simple’ and logical ingenious reasoning!
Carnot’s reasoning proves that a reversible cycle cannot have a lower efficiency (power output relative to heat input) than any other cycle, thus all reversible cycles must have the same maximum possible power–efficiency for the given temperatures of the two thermal reservoirs, independently from anything else, including the nature of the heat engine design and its agent undergoing the cyclic process (see all relevant specifics in [
1,
9,
10] and elsewhere; see also
Key Point V and
Key NOVEL-Point 2).
Since the irreversible cycles could not be reversed, they may (and do) have lower than maximum reversible efficiency up to zero (no net work produced, if all work potential is dissipated to heat) or even negative (external work input required to run such a “parasite” engine that will dissipate such work into heat, in addition to the original work potential dissipation), i.e.:
Carnot did not provide a quantitative, but a qualitative correlation for the ideal heat engine power–efficiency. Note that this combined, empirical efficiency (“net work output per heat input”) includes not only heat engine but also the heat reservoirs, and in that regard is misleading (see
Key NOVEL-Point 4). Sadi Carnot accurately specified all conditions that must be satisfied to achieve reversibility and the maximum efficiency: the need for “
re-establishing temperature equilibrium for caloric transfer”, i.e., reversible processes, where the reversible heat transfer has to be achieved at a negligibly small (in the limit of zero) temperature difference at both temperature levels, at
TH, high temperature for heat source (reversible heating), and at
TL, low temperature for heat sink (reversible cooling of heat engine medium), see
Figure 2 and
Figure 3, otherwise the work potential during the heat transfer will be irreversibly lost due to the temperature difference (the main Carnot
cause-and-effect reasoning), see also
Key Point II.
Sadi Carnot reasoned that mechanical expansion and compression are needed to decrease and increase the temperature of the engine medium to match the low and high temperature of the thermal reservoirs, respectively, and thus provide for the reversible heat transfer [
1].
Carnot then reasoned that in limiting cases, such as an ideal cycles, it could be reversed using the prior obtained work, to transfer back the caloric (heat) from low- to high-temperature thermal reservoirs, thus laying the foundations for the refrigeration cycles (cooling and refrigeration/heat pumps) as ‘reversed’ heat engine cycles, see
Figure 3 and Equation (2).
Sadi Carnot’s reasoning of “
heat engine reversible cycles and their maximum efficiency” is importance-wise on par with Einstein’s
Relativity theory in modern times, see Equation (4). It may be among the most important correlations in natural sciences that led to the discovery of
entropy and the
Second Law of thermodynamics, among others. This claim was stated by this author, ‘symbolically’ expressed by Equation (4), and named as the ‘
Carnot (ratio)
Equality’ in prior publications [
9,
11] to emphasize the invaluable but not well-recognized importance of the
Q/T =
constant correlation, renamed here as ‘
Carnot-Clausius Equality’, as the precursor to and to resemble the ‘
Clausius Equality’ cycle integral, both formalized by Clausius [
7] based on Carnot’s
Réflexions [
1].
The ‘
Key Reflections’ presented next are founded on Sadi Carnot’s ‘
Réflexions’ (English translation by Robert H. Thurston [
1] and elsewhere) and on the developments of thermodynamics by the pioneers [
6,
7] and others, emphasizing this author’s views as a lifelong engineering thermodynamicist [
5,
8,
9,
10,
11] as a complement to existing science historians and science philosophers’ analyses, e.g., [
12,
13,
14,
15,
16].
Therefore, a key thermodynamic logic is used to recognize and infer the most probable sequential developments of Sadi Carnot’s ingenious discoveries, as well as to reflect on the related analyses and misconceptions by others, considering the current state of knowledge—since now, we have the advantage to look at the historical developments more comprehensively and objectively than the pioneers. The sequential ‘Key Points’, where key reasoning by Sadi Carnot infers the next one, along with ‘Miss Points’ (persistent post-misconceptions and fallacies by others), including novel contributions and original generalizations by this author, as ‘Key NOVEL-Points’ with ‘Key Takeaways’, are presented next.
3. Miss Points: Persistent Post-Misconceptions and Fallacies by Others
The well-known Carnot efficiency formula,
, was not established by Sadi Carnot, but much later by Kelvin and Clausius;
The cause and source for motive power is the temperature difference, in principle, but is not linearly dependent, as mis-stated by some;
The heat transferred out of the Carnot cycle at a lower temperature is “not a waste heat” as often stated, but it is a “useful quantity”, necessary for the completion of the cycle;
Sadi Carnot could not have been thinking of “any other caloric” but heat to imply “entropy-like quantity”, as speculated by some.
Miss Point 1: The well-known Carnot efficiency formula, , was not established by Sadi Carnot, but much later by Kelvin and Clausius.
In 1824, Sadi Carnot inferred the maximum heat engine power efficiency as an implicit function of thermal source and sink reservoirs’
high and
low, tH and
tL, temperatures only [
]. Note that the absolute temperature concept was not known at that time. However, the well-known
Carnot efficiency formula,
, with absolute temperature, sometimes attributed as having been developed by Sadi Carnot, was actually developed much later, in the 1850s, first by Kelvin [
6] using ideal gas, and later by Clausius [
7] in general, and named “
Carnot efficiency”.
Paradoxically, it is shown here that Carnot, Kelvin, and Clausius’ concepts of the maximum reversible cycle efficiency are misplaced, since fundamentally, the Carnot cycle efficiency is not the “reversible cycle efficiency” per se, but a power-per-heat ‘coefficient of performance, COP < 1’, that includes both the heat engine and thermal reservoir efficiencies, to be decoupled, see Key NOVEL-Point 4. It is fundamentally like its inverse, the heat-per-power COP > 1 of the heat pump. Essentially, it is a thermal energy source ‘work-potential efficiency’—see more details in Key NOVEL-Point 4. After all, the Carnot cycle efficiency does not depend on the cycle in any way, but on the thermal reservoirs’ temperatures only.
Miss Point 2: The cause and source for the motive power is the temperature difference, in principle, but is not linearly dependent, as misattributed by some.
Carnot stated that the temperature difference is, in principle, the cause and source for the motive power, but not directly, linearly dependent, as misquoted by some [
), i.e., not the function of Δ
t =
]. As stated by Sadi Carnot, “
In the fall of caloric the motive power undoubtedly increases with the difference of temperature between the warm and the cold bodies; but we do not know whether it is proportional to this difference. … The fall of caloric produces more motive power at inferior than at superior temperatures” [
1].
Miss Point 3: The heat transferred out of the Carnot cycle at a lower temperature is “not a waste heat” as often stated, but it is a “useful quantity”, necessary for the completion of the cycle.
The heat transferred out of the ideal Carnot cycle at a lower temperature is “
not a waste” as often stated, but necessary for the completion of the cycle (the entropy balance), and therefore necessary and a
useful quantity. As stated by Sadi Carnot, “
… without ‘the cold’ the heat would be useless [
1] (see also elswhere)”. The only waste is the additional heat generated via irreversible work dissipation, accompanied by
entropy generation in real cycles, which must also be taken out to complete the cycle.
Miss Point 4: Sadi Carnot could not have been thinking of “any ‘other’ caloric” but heat to imply the “entropy-like quantity”, as speculated by some.
We need to keep in mind that in Sadi Carnot’s time (the early 1800s), the steam engines were inefficient (below 5%, so the heat in and heat out were comparable within experimental uncertainty, as if caloric is conserved), the conservation of caloric flourished, and many critical thermal concepts, including the conservation of energy (The First Law), were not even established. At that time, the entropy concept was not even remotely known. Therefore, Sadi Carnot could not have been thinking of “any ‘other’ caloric” but heat to imply the “entropy-like quantity”, as speculated by some—see Key NOVEL-Point 6 for more details.
Novel contributions with deeper physical insights and related generalization by this author are formalized in the following ‘Key NOVEL-Points’.
4. Key NOVEL-Points: Novel Contributions and Original Generalizations
“Reversible and Reverse” Processes and Cycles Dissected;
Maximum Efficiency and “Reversible Equivalency” Scrutinized;
Reversible Contradiction Impossibility (“Reductio ad absurdum”);
Reversible Carnot Cycle Efficiency Is Misplaced—It is NOT the “Cycle efficiency” ‘per se’, but a “Thermal energy-source ‘work-potential efficiency’”;
The Carnot–Clausius [Ratio] Equality (CCE) and Clausius Equality (Cyclic integral) are special cases of relevant “Entropy boundary integral” for reversible stationary processes;
The ‘caloric’ is transformable to work and cannot be ‘extended and renamed as entropy’, which is ‘the final transformation’.
Key NOVEL-Point 1: “Reversible and Reverse” Processes and Cycles Dissected.
Ideal and perfect “Reversible processes” take place at infinitesimal potential differences (temperature, pressure, and similar) at any instant within and between a system and its boundary surroundings, but they may and do change in time (process is a change in time). Namely, the spatial gradients are virtually zero at any instant, while the time gradients and related fluxes may be arbitrary, as they are driven by ideal boundary surroundings and facilitated by ideal arbitrary (or infinite) transport coefficients. Therefore, the potential qualities of the flux quantities (heat and different kinds of works) are not degraded, but equipotentially transferred and stored between the system and its boundary surroundings, and thereby ‘truly’ conserved in every way. However, in time, due to the unavoidable irreversible dissipation of work to the generated heat, accompanied by a generation of entropy, all real processes between the interacting systems (including the relevant surroundings) are asymptotically approaching the common equilibrium with zero mutual work potential and maximum mutual entropy.
Namely, if an elastic, ideal gas, or ideal spring is reversibly compressed, then the pressure may change in time, but is equal everywhere at any instant across the system and the boundary surroundings (equipotential driving force at any instant). Similarly, if the heat is reversibly transferred, the temperature may change in time, but it is equal everywhere within the system at any instant, and if it varies in time, it is driven by the varying, but spatially equipotential surrounding temperature, so that the energy potential quality is stored and conserved everywhere in every way (it may be reversed back-and-forth in perpetuity without additional external compensation).
Note that the ‘time and energy-rates’ are irrelevant, per se, for the reversible analysis of energy balances and properties between the initial and final states, being independent of the process type and path of how the final state is achieved, either reversibly or irreversibly, the former being simpler and more suitable for analysis than the latter.
A Cycle is a special case of a quasi-stationary process when the flow inlet and outlet quantities are the same (feed into each other) and close the cycle. Like a stationary process, a cycle does not accumulate flux quantities and may repeat and last in perpetuity (quasi-stationary). Note that all processes, particle-wise, are transient in time (in the Lagrangian sense, from the inlet to the outlet), but for the steady-state or stationary processes (in the Eulerian sense), the properties do not change in time (zero temporal gradients) at a fixed location, and for a cyclic process, the flow inlet’s quantities are the same as the outlet’s (since they feed into each other).
A “Reverse” concept is independent of and should not be confused with the reversible concept. If reversible, a reverse process could be reversed using prior, related process work (with an infinitesimal change in the potential difference in opposite directions, and without additional external work compensation), while to reverse an irreversible process, it would require additional, external work compensation.
A “
Reverse process” and/or “
Reverse cycle” would take place if the driving (forced) potentials of a reversible process or a cycle were reversed (by an infinitesimal change in opposite directions), then such a reversible process would be reversed with all the quantities changing direction from the input to output (and vice versa, e.g., a
refrigeration cycle is a “
reverse” of a
power cycle or vice versa, see Equation (2) and
Figure 3). For stationary processes, there are no temporal gradients or accumulation of flux quantities within a system, and for quasi-stationary cycles, there is no accumulation of flux quantities after the completion of a cycle. The input and output quantities would be conserved and could be
reversed back-and-fort in perpetuity like a perpetual motion.
In reality, there is a need for at least an infinitesimal temperature difference (and/or pressure and similar) to provide a process ‘sense of direction’, and to resolve directional ambiguity by chance. Therefore, every process must be at least infinitesimally irreversible (infinitesimally imperfect), with the reversibility being an asymptotic, limiting ideal concept. For this reason, even a reversible equilibrium is unachievable; like an absolute zero temperature or any other ideal concept, it can only be approached asymptotically.
Key NOVEL-Point 2: Maximum Efficiency and “Reversible Equivalency” Scrutinized.
The maximum efficiency of an energy process or cycle entails the
maximum possible work extraction from a system while coming to an equilibrium with a reference system, usually the surroundings; or the
minimum possible work expenditure in a
reverse process of the formation of original system (from within the same reference state), see
Figure 4—
Center. Since the reversible processes do not degrade any potential quality and could be reversed without external intervention, the two works must be the same, with opposite signs only, for all reversible processes, and they represent the maximum
work potential (WP) for the given non-equilibrium conditions. Therefore, the reversible processes are perfect, and
equally and maximally 100% efficient. They define the concept of “
Reversible Equivalency”—the
‘true quantity and quality equality’ of input and output, where relevant quantities and qualities are conserved in perpetuity. In real processes, there will be some work dissipation losses (degradation of work with its dissipative conversion to heat), so that
less work would be extracted than the maximum possible, and
more work would be needed than the minimum required, thus reducing the maximum possible efficiency for real,
irreversible processes (see Equation (3) and
Figure 4—
Left). The reversible processes take place in virtual equipotential conditions (virtually the same temperature, pressure, etc.; they are equipotential locally at any time, thus being reversible at any time), but they may vary in time with time-variable systems and surrounding properties. Therefore, the ‘potential quality’ of all relevant quantities would be equipotentially transferred and stored at any time, i.e., conserved without any degradation (without any dissipation) and could be effortlessly reversed back-and-forth (without additional external compensation).
With the infinitesimal reversal of the relevant potentials, all flux quantities will change directions while conserving the quantities and qualities. Therefore, the work extraction in a
reversible cycle (i.e., work potential, WP) would be equal to the expenditure or formation work in its ‘
reverse’
reversible cycle (see Equation (2) and
Figure 3 and
Figure 4). Furthermore, all reversible cycles must have an equal and maximum 100% efficiency, otherwise any
‘under-achieving’ reversible cycle (with lower work extraction than another [reference] cycle), when reversed, would consume less work than the reference cycle, and thus be
‘over-achieving’ with a higher-than-reference 100% maximum efficiency, resulting in a ‘
Contradiction impossibility’, see
Key NOVEL-Point 3 next.
Key NOVEL-Point 3: Reversible Contradiction Impossibility (“Reductio ad absurdum”).
As stated above, the reversible efficiency implies the
maximum work extraction and
minimum work expenditure in the reverse process; therefore, the two must be equivalent for the given conditions, thus establishing the
Reversible Equivalency, see also
Key NOVEL-Point 2. Otherwise, any reversible cycle “
under-achievement” (obtaining less than the maximum possible) would become an “
over-achievement” when such a cycle is reversibly ‘reversed’ (accomplishing with less than the minimum required), and such a “
reverse over-achievement” would be physically impossible—it would be the “
Reversible Equivalency violation” and may violate the
conservation laws, thus implying the “
Reversible Contradiction Impossibility” of a well-known fact, see
Figure 4—right (impossible
‘miracle GAIN’).
Namely, the “
Reversible Contradiction Impossibility” (an
under-achieving reversible process when reversed) would become an
impossible over-achieving reversible process and could result in numerous consequences. Namely, the miraculous creation of ‘perpetual motion’ or the creation of an assumed ‘conserved caloric’ (regardless of Sadi Carnot’s misconception of
caloric conservation) and other impossible processes, like spontaneous heat transfer from lower to higher temperatures, etc. The ‘Reversible Contradiction Impossibility’ is so strong and universal a concept that any pertinent or quasi-relevant criteria, even if misunderstood, like the conservation of caloric, will be sufficient to reason fundamental inferences [
1].
Further consequences of the “
Reversible Contradiction Impossibility” would be the spontaneous generation of a conserved quantity, or the generation of non-equilibrium work potential, or energy transfer from a lower to higher potential, like spontaneous heat transfer from a lower to higher temperature and the generation of a thermal non-equilibrium, i.e., the impossible destruction of entropy, see more details in [
9,
10,
11] and elsewhere. Or, in general, the spontaneous creation of a non-equilibrium from within an equilibrium being the physical contradiction of the always observed “spontaneous process, forcing-direction from non-equilibrium towards mutual equilibrium,” and never experienced otherwise. It will amount to the “
forced-
directionality contradiction” of the
irreversible process directionality from a higher to lower potential towards mutual equilibrium, as well as the
impossibility to reverse dissipation.
KEYNOTE 2: It would be logically and otherwise impossible and absurd (“Reductio ad absurdum”) to have a spontaneous process “the one way and/or the opposite way” arbitrarily in opposite directions, by chance (i.e., to have heat transfer “from hot-to-cold or from-cold-to-hot” or “forcing in one direction and accelerating in opposite direction,” by chance). It would be a violation of the Second Law of thermodynamics (2LT). |
The reversible processes are equipotential and therefore do not degrade a non-equilibrium, but store and/or convert one kind to another, like a reversible cycle converts ‘
heat at high temperature’ to ‘
work plus heat at lower temperature’, and in reverse in perpetuity, defined in [
11] as the “
Carnot-Clausius Heat-Work Equivalency, CCHWE” (‘potential-like’ heat at a high temperature is equivalent and converts to ‘kinetic-like’ work plus heat at lower temperature, and vice versa—analogous to a reversible pendulum, converting potential to kinetic energy, and in reverse, in perpetuity), see
Figure 5. The
CCHWE is a fundamental and autonomous physical concept, independent of any process or device [
11].
Therefore, all reversible processes are perfectly “equivalent in every way” and the most efficient, without any dissipative degradation.
Key NOVEL-Point 4: Reversible Carnot Cycle Efficiency Is Misplaced—It is NOT the “Cycle efficiency” ‘per se’, but a “Thermal energy-source ‘work-potential efficiency’”.
The reversible processes and cycles, as a matter of concept, are 100% perfect without any degradation and must be equally and perfectly (maximally) efficient, not over nor below 100% efficiency (would be the
Reversible Contradiction Impossibility). Therefore, all reversible processes and cycles have 100% “true quantity and quality” efficiency—they extract 100% of the “available work potential”, as does any ideal waterwheel and any other reversible energy transformer (e.g., engine or motor). The 100% perfect “true reversible efficiency” [11 (
CCHWE)], see
Figure 6—
Right, should not be confused with the “maximum work-thermal efficiency” of a thermal energy source, which represents the “work potential of heat” or Exergy of heat (or non-equilibrium thermal energy) of the relevant thermal reservoirs [
Ex =
WRev|Max =
Q(1 −
T0/
TH), where
TC =
T0], see
Figure 6—
Left, as their property-like quantity, being independent of any heat engine or energy device.
Sadi Carnot [
1] and his followers, including Kelvin [
6] and Clausius [
7], ironically referred to the maximum heat engine cycle efficiency (that they “agonizingly” developed at the time, when most thermal concepts were unknown) with the
absurd conclusion that “
it does not depend on the cycle design itself nor its operation mode [in any way whatsoever]”, hence, it is not related to the cycle in any way, which is the proof that it is not the efficiency of the ideal Carnot cycle
per se. Therefore, their attribution is misplaced, since the efficiency they developed
should have referred to the “maximum motive power or
‘work potential (WP)’ of the thermal reservoirs” since it depends on their temperatures only, hence, being the logical proof of the claim presented here.
KEYNOTE 3: Carnot heat engine efficiency dependence on the temperatures of the heat reservoirs would only be equally misplaced as if to attribute the maximum efficiency of an ideal waterwheel (water turbine), based on its motive power per unit of input water flow, and then it would also mistakenly depend on the water reservoirs’ elevations only. Therefore, all reversible devices are and have to be equally (not below nor above) the maximum possible 100% efficiency. |
A motive power efficiency (i.e., a device’s work efficiency) should be consistently based on the work potential of an energy source (not on a “convenient nor arbitrary input quantity,” like the heat input or water flow input, etc.), and then, the ‘true’ Carnot cycle efficiency would be 100%, as for all the other efficiencies for ideal, reversible engines and motors.
Sadi Carnot defined engine cycle efficiency, logically and “empirically,” as “[work] motive-power
output per heat
input”, long before the concepts of the “
work potential” of an energy source and
energy conservation were established. However, we now have the advantage of looking at the historical developments more comprehensively and objectively than the pioneers [
5,
8,
9,
10,
11], to put in order historical misconceptions.
An exact “
reverse” of the reversible “
Power Carnot-cycle” is the ideal “
Heat-pump cycle” (“
Reverse Carnot-cycle”), whose efficiency or “performance” is defined ‘in inverse’ as “heat
output per work
input”. It is always over 100% (as the “fundamental inverse” of the
Carnot cycle efficiency, with the latter, as defined, always smaller than 100%), and it is named as the “
Coefficient of Performance (COP)” since ‘such efficiency’ over 100% would not be fundamentally (nor “politically”) proper, but it should be fundamentally the same, i.e., improper also if smaller than 100%.
KEYNOTE 4: For the same fundamental reason, the efficiency of a perfect, ideal Carnot cycle (being below 100%) would also be logically inappropriate (as if there are “some work losses” in the ideal reversible cycles). For the same reason as for the Heat pump cycle, it should be called the ‘Carnot cycle COP’, not the ‘Cycle efficiency’. Fundamentally, all ideal, reversible cycles must be “equally and maximally [100%] efficient,” as reasoned by Sadi Carnot [1]. |
Furthermore, it is fundamentally inappropriate, as often stated, to call the heat transferred out of the Carnot cycle at a lower temperature, the “
waste heat or
loss”, since it is the “
useful quantity,”
necessary for the completion of the perfect, ideal cycle. Together with the cycle work, they are reversibly transformable (interchangeable as equal) and present the “
reversible equivalent” to the heat input at the high temperature, named by this author as the
Carnot–Clausius Heat Work Equivalency (
CCHWE) [
11]), a crucially fundamental and autonomous concept (independent of any process or device), see also
Figure 5. The only “waste or loss” that could lower efficiency below 100% would be any ‘
irreversible work dissipation’ (converted into generated heat) and accompanied by
entropy generation, which must also be taken out to complete a real cycle. A device’s efficiency could not be higher than 100%, and it could only be lower due to irreversible, dissipative losses.
The “original,”, nowadays well-known Carnot cycle efficiency is misplaced and inappropriate, and it should be renamed for what it is: the Work potential (WP, or ‘available energy’) efficiency of a heat source and sink, or Exergy efficiency of a thermal energy source with respect to the heat sink reference. We now know that the “true” Carnot efficiency, the Second Law or Exergy efficiency, is 100%. It is a goal here to clarify and rectify what is fundamentally misplaced. However, it would be hard “to let go” of the 200-year-long “habit and addiction”.
Key NOVEL-Point 5: The Carnot–Clausius [Ratio] Equality (CCE) and Clausius Equality (Cyclic integral) are special cases of a related “Entropy boundary integral” for reversible stationary processes.
The balance equations (used for the definition of a new property, the entropy) were first developed by Clausius, based on Carnot’s discovery of “maximum efficiency and equality for all reversible cycles”, named here the Carnot–Clausius Equality, CCE, as the ratio QH/TH = QL/TL for the constant high and low temperature of the thermal reservoirs, to be the precursor of Clausius Equality, as a circular integral for a reversible cycle with variable temperatures, . Then, from those correlations, a new property, entropy, was inferred by Clausius, to be later generalized with Clausius Inequality as the entropy balance, as a “quantification” of the Second Law of thermodynamics.
The
Carnot–Clausius Equality (
CCE, as finalized and renamed here to reconcile and streamline it with the cyclic
Clausius Equality, was named the
Carnot [Ratio] Equality,
CtEq, in [
11]) is, in essence, the entropy balance, i.e., “
entropy-in equal to
entropy-out” of the reversible Carnot cycle at constant in and out temperatures, while the
Clausius Equality is also the balance of the net entropy (
in-minus-out) of a reversible cycle with varying temperatures, a cyclic integral around the cycle boundary or per cycle time period. They both represent special cases of the
entropy balance for the steady-state, stationary processes (including quasi-stationary cyclic processes), where there is no accumulation of entropy (nor accumulation of any other system properties).
Note that engines are designed to run and produce power perpetually (except for necessary maintenance and repair). Therefore, their processes have to be either steady-state (stationary processes) or quasi-steady cyclic processes, often achieved by rotating or reciprocating piston and cylinder machinery, or any similar energy conversion devices. Neither steady-state nor cyclic processes accumulate mass and energy, but convert input to output while interacting with the energy reservoirs, an energy source and reference sink, the latter usually a surrounding device.
Key NOVEL-Point 6: The ‘caloric’ is transformable to work and cannot be ‘extended and renamed as entropy’, which is ‘the final transformation’.
It is stated in
Miss Point 4 that “Sadi Carnot could not have been thinking of ‘any ‘other caloric’ but heat to imply the ‘entropy-like quantity’, as speculated by some”. There are creative and persuasive publications, albeit with fundamental deficiencies, that try to draw attention to and establish new interpretations of the caloric concept, first to ‘cancel’ its original meaning as “heat” (e.g., “Heat is not a noun” by Romer), and more recently as “Extended Caloric Theory” and to “make caloric equivalent to entropy”, as well as to generalize Carnot’s ‘waterfall analogy’ as the ‘Archetype of Waterfalls’ [
16].
However, some critical statements are inconsistent with thermodynamic fundamentals. Namely, “
So, ‘any restoration of equilibrium in the caloric’ simply means any fall of caloric through a temperature difference” [
16]”. This is elusive and, in general, misplaced, since Carnot referenced the “restoration of equilibrium of caloric” via the reversible extraction of the motive power, as in an ideal heat engine, and not “any fall of caloric” like in an irreversible heat transfer from a high to low temperature in heat exchangers. Sadi Carnot also stated “
the need for reestablishing temperature equilibrium [using adiabatic compression or expansion]
for [isothermal/reversible]
caloric transfer” (
Key Point II). Furthermore, “
The authors’ motivation has been to make clear that an Extended Caloric Theory that allows for production of caloric, makes caloric equivalent to entropy in macroscopic thermodynamics [
16]”. This is misplaced and fundamentally incorrect. For example, the
caloric may in part be isentropically converted to work and reduced (as in Carnot heat engine; entropy conserved), or dissipated to a lower temperature and conserved (as in a heat exchanger, while entropy will not be conserved); hence, the two are not the same (see also next and elsewhere).
Therefore, the
caloric/heat is not equivalent to
entropy; the latter is irreversible and the ‘
final transformation’ (it is not possible to convert entropy to anything else—not possible to ‘destroy’ entropy), while the dissipative heat generation and/or conversion of heat to/from work, is not the ‘final transformation’ (caloric/heat could be increased or decreased, via a heat pump or heat engine, respectively, or generated by work dissipation). Furthermore, entropy is related to caloric (heat); the latter is the conjugate product of entropy (extensity) and temperature (intensity) [
11]. It would be analogous and incorrect to claim that in a
waterwheel the ‘water flow work’ is equivalent to the ‘water volume flow’, since ‘work’ is the conjugate product of ‘volume (extensity)’ and ‘pressure (intensity)’. Again, the caloric may be in part converted to work and vice versa (in “
thermal transformers” i.e., heat pumps and heat engines) and thus overall increased or reduced, but the latter is not possible for entropy. Furthermore,
heat (caloric) and
work are reversibly transformable (interchangeable as equivalent), as formalized as the “
Carnot-Clausius Heat-Work Equivalency (CCHWE)”, i.e., ‘heat at high temperature’ is (reversibly) equivalent, i.e., transformable to ‘work plus heat at low temperature’ and vice versa. As already stated, the
CCHWE is a fundamental and autonomous physical concept, independent of any process or device [
11], see also
Figure 5.
Therefore, the caloric (thermal energy) is not entropy (thermal displacement/space). Certainly, conserved ‘caloric’ at Carnot’s time was known as the present name ‘heat’, which is extensively used in calorimetry nowadays, with “calorie” still being used as a heat unit, especially in chemistry and life.