<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">JMP</journal-id><journal-title-group><journal-title>Journal of Modern Physics</journal-title></journal-title-group><issn pub-type="epub">2153-1196</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/jmp.2014.516159</article-id><article-id pub-id-type="publisher-id">JMP-50604</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Physics&amp;Mathematics</subject></subj-group></article-categories><title-group><article-title>
 
 
  Thermodynamics and Irreversibility: From Some Paradoxes to the Efficiency of Effective Engines
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>livier</surname><given-names>Serret</given-names></name><xref ref-type="aff" rid="aff1"><sub>1</sub></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib></contrib-group><aff id="aff1"><label>1</label><addr-line>ESIM Engineer—60 rue de la Marne, Cugnaux, France</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>o.serret@free.fr</email></corresp></author-notes><pub-date pub-type="epub"><day>17</day><month>10</month><year>2014</year></pub-date><volume>05</volume><issue>16</issue><fpage>1575</fpage><lpage>1593</lpage><history><date date-type="received"><day>5</day>	<month>August</month>	<year>2014</year></date><date date-type="rev-recd"><day>2</day>	<month>September</month>	<year>2014</year>	</date><date date-type="accepted"><day>27</day>	<month>September</month>	<year>2014</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/</license-p></license></permissions><abstract><p>
 
 
  The traditional thermodynamic theory explains the reversible phenomena quite well, except that reversible phenomena are rare or even impossible in practice. Here the purpose is to propose an explanation valid for reversible and also irreversible phenomena, irreversibility being common or realistic. It previously exposed points tricky to grasp, as the sign of the work exchange, the adiabatic expansion in vacuum (free expansion) or the transfer of heat between two bodies at the same temperature (isothermal transfer). After having slightly modified the concepts of heat transfer (each body produces heat according to its own temperature) and work (distinguishing external pressure from internal pressure), the previous points are more easily explained. At last, an engine efficiency in case of irreversible transfer is proposed. This paper is focused on the form of thermodynamics, on “explanations”; it does not question on “results” (except the irreversible free expansion of 1845...) which remain unchanged.
 
</p></abstract><kwd-group><kwd>Heat Transfer</kwd><kwd> External and Internal Pressure Work</kwd><kwd> Internal Energy</kwd><kwd> Reversible and Irreversible</kwd><kwd> Joule’s Law and Joule’s Experiments</kwd><kwd> Adiabatic and Free Expansion</kwd><kwd> Clapeyron Diagram</kwd><kwd> Carnot Cycle</kwd><kwd> Engine Efficiency</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Thermodynamics traditionally [<xref ref-type="bibr" rid="scirp.50604-ref1">1</xref>] [<xref ref-type="bibr" rid="scirp.50604-ref2">2</xref>] deals of relations between the thermal and the mechanical phenomena. It is a science that was born in the nineteenth century and was codified by scholars as Sadi CARNOT or James Prescott JOULE. Since then, little major changes have been made, on form and content. It is on this first point that presentation takes place in this essay. Indeed, some statements remain difficult to understand, even if current “explanations” do not taint the veracity of the “results”.</p><p>In the first part, we will check some statements tricky to understand: a mathematical equality considered as a physical principle, an expansion without any work, a negative work represented by a positive area, a transfer of heat between two bodies at the same temperature, and a cycle where heat seems to go from cold to hot! In the second part, we will change the forms of the heat transfer and of the work and consequently of the internal energy. Then in the third part, we will apply these new forms to the first statements which were tricky to understand. Explanations look then more understandable, especially for irreversible phenomena. At last, an efficiency ratio based on differences of temperatures is proposed for irreversible cycles.</p></sec><sec id="s2"><title>2. Some Statements Tricky to Understand</title><sec id="s2_1"><title>2.1. The “Principle Zero” of Thermodynamics</title><p>Its name or more precisely its numbering—“zero”—is unusual. The reason is historical. The first principles having already been laid, it has nevertheless been considered necessary to add another one prior to the demonstrations. But more than its numbering, it is its content which is surprising as a “principle”. Recall that the principle zero states that if A is in (thermal) equilibrium with B and B with C, then A is with C. This is surprising because that looks like more to a mathematical property (a transitive law, an equivalence relation or an axiom as “two quantities equal to a third are equal”) than to a physical principle. In other branches of physics, it is not stated as a “principle” that if A has the same mass as B and B as C, then A has the same mass as C. This zero principle asks a question: does not it reflect a certain difficulty in characterizing thermal equilibrium?</p></sec><sec id="s2_2"><title>2.2. Free Expansion and Joule Experiment</title><sec id="s2_2_1"><title>2.2.1. Historical</title><p>In 1806, Louis GAY-LUSSAC was the first to experiment expansion in vacuum. Measuring the temperature directly on the air with an alcohol thermometer, he found no variation of temperature [<xref ref-type="bibr" rid="scirp.50604-ref3">3</xref>] .</p><p>In 1845, James JOULE did the same experiment, except that it measured the temperature of the surrounding water; he found no variation of temperature either [<xref ref-type="bibr" rid="scirp.50604-ref4">4</xref>] .</p><p>In 1865, Gustave-Adolphe HIRN did the same experiment, measuring the temperature through a variation of pressure. He found a light variation of temperature: −0.2˚C [<xref ref-type="bibr" rid="scirp.50604-ref5">5</xref>] . See <xref ref-type="fig" rid="fig1">Figure 1</xref>.</p><p>Since there, the experiment has been done again with carbon dioxide CO<sub>2</sub> (which is more sensitive than air): it has been noted a decrease of temperature of −0.3˚C [<xref ref-type="bibr" rid="scirp.50604-ref6">6</xref>] [<xref ref-type="bibr" rid="scirp.50604-ref7">7</xref>] .</p><p>And today, it is mainly the usual industrial way to cool gases [<xref ref-type="bibr" rid="scirp.50604-ref8">8</xref>] [<xref ref-type="bibr" rid="scirp.50604-ref9">9</xref>] .</p><p>And yet History has retained the result of the Joule’s experiment with no variation of temperature!</p></sec><sec id="s2_2_2"><title>2.2.2. Explanation</title><p>Let us remind that an ideal gas is a gas that obeys the ideal gas law:</p><disp-formula id="scirp.50604-formula1785"><label>(1)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x5.png"  xlink:type="simple"/></disp-formula><p>with P: internal pressure of the gas; V: volume of gas; n: amount of substance of the gaz (in moles); R: gaz constant (8.314 J&#183;K<sup>−</sup><sup>1</sup>&#183;mol<sup>−</sup><sup>1</sup>); T: absolute temperature (in Kelvin).</p><p>This is a good approximation for gases in usual conditions (when the pressure is relatively low, less than 10 atm.) like the atmospheric pressure. It is often used to describe cycles, compressions and expansions.</p><p>There are two laws of Joule: the first one called Joule-Gay Lussac law and the second one called Joule- Thomson law. The first law states that for ideal gas the internal energy depends only on the temperature, the</p><fig id="fig1"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref></label><caption><title> The so-called Joule’s experiment</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x6.png"/></fig><p>second one that the enthalpy depends only on its temperature. To check it, these scholars set up an experiment showing that “the gas temperature would remain constant” (which is quite different to the Joule’s law: U depends only on its temperature) with the expansion, due to the formula</p><disp-formula id="scirp.50604-formula1786"><label>(2)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x7.png"  xlink:type="simple"/></disp-formula><p>The reasoning is as follow: because there is no heat transfer, and because there is no work (<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x8.png" xlink:type="simple"/></inline-formula>so without external pressure, there would not be pressure work), there is no change of internal energy U and so we should not have change of temperature.</p><p>This is why it is still traditionally explained that if the gas cools in experiments, it is that in sudden expansion the gas is far to be ideal [the gas would not obey to Equation (1)]: this is an indirect recognition that traditional theory is not in agreement with experimental results...</p></sec><sec id="s2_2_3"><title>2.2.3. A Surprising Result</title><p>What a surprising result: a thermodynamic system which keeps constant its internal energy U and its temperature T, and which does not receive any heat or work but submits an irreversible change! It is the result found by Pr. Joule in 1845.</p><p>Why is it qualified here of surprising result? Because it is unusual to get:</p><p>&#183; no work when the volume changes; it would be surprising that the border line, which can be the black top of <xref ref-type="fig" rid="fig1">Figure 1</xref>, moves without any work! It would be at variance with the first principle of thermodynamics where perpetual motion machines of the first kind are impossible...</p><p>&#183; a constant temperature</p><disp-formula id="scirp.50604-formula1787"><label>(3)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x9.png"  xlink:type="simple"/></disp-formula><p>when in the reversible and in the other irreversible cases, the temperature decreases [<xref ref-type="bibr" rid="scirp.50604-ref10">10</xref>] with expansion (without heat transfer); please check on <xref ref-type="fig" rid="fig2">Figure 2</xref>.</p></sec></sec><sec id="s2_3"><title>2.3. Work Representation by Its Area</title><p>In mathematics, the area is calculated by integrating a function. If the function <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x10.png" xlink:type="simple"/></inline-formula> is positive so its integral, represented by an area, is positive: <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x11.png" xlink:type="simple"/></inline-formula>[<xref ref-type="bibr" rid="scirp.50604-ref11">11</xref>] . See <xref ref-type="fig" rid="fig3">Figure 3</xref> where <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x12.png" xlink:type="simple"/></inline-formula> is <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x13.png" xlink:type="simple"/></inline-formula> and <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x14.png" xlink:type="simple"/></inline-formula> is<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x15.png" xlink:type="simple"/></inline-formula>.</p><p>In thermodynamics, work is conventionally counted positively when received and negatively when provided by the system. The infinitesimal work exchanged by the system is denoted<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x16.png" xlink:type="simple"/></inline-formula>.</p><disp-formula id="scirp.50604-formula1788"><label>(4)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x17.png"  xlink:type="simple"/></disp-formula><p>The pressure <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x18.png" xlink:type="simple"/></inline-formula> being always positive, when V<sub>2</sub> is higher than V<sub>1</sub> (that is, when x<sub>2</sub> higher than x<sub>1</sub>), the thermodynamics sum W is then negative:<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x19.png" xlink:type="simple"/></inline-formula>. How explain that in the [P-V] Clapeyron diagram particularly suitable for representation of work, the negative work W is paradoxically represented by a positive area<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x20.png" xlink:type="simple"/></inline-formula>?</p></sec><sec id="s2_4"><title>2.4. Carnot Cycle</title><p>The theorizing of thermodynamics by physicists did not precede but followed or accompanied the development by engineers of thermal engines as the steam engine. They had already realized that the efficiency <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x21.png" xlink:type="simple"/></inline-formula> (work</p><fig id="fig2"  position="float"><label><xref ref-type="fig" rid="fig2">Figure 2</xref></label><caption><title> Work and temperature evolution with expansion</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x22.png"/></fig><fig id="fig3"  position="float"><label><xref ref-type="fig" rid="fig3">Figure 3</xref></label><caption><title> Representation of positive mathematical area</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x23.png"/></fig><p>done/energy transmitted by the hot source) seemed limited by an unsurpassable value related to the temperatures of the sources.</p><disp-formula id="scirp.50604-formula1789"><label>(5)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x24.png"  xlink:type="simple"/></disp-formula><p>Was it an impression or a physical principle? Sadi Carnot, who thought the heat was a fluid called caloric, described a clever cycle (not representative of an existing machine) which reaches the performance limit. Let us consider a transformation of this cycle, the isothermal transformation. See <xref ref-type="fig" rid="fig4">Figure 4</xref>.</p><p>An isothermal transformation is a transformation that takes place at constant temperature, in contact with a thermostat. Take for example a piston air-filled at 20˚ Celsius, in an external medium like water also at 20˚ Celcius. The air volume is adapted to the pressure according to the ideal gas law. This system is in stable equilibrium; it does not change and will not change spontaneously. And there is no reason that for two bodies at the same temperature, heat flows in one direction rather than another. In the case of perfect equality between fluid temperature and thermostat temperature: there is no transfer of heat.</p><disp-formula id="scirp.50604-formula1790"><label>(6)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x25.png"  xlink:type="simple"/></disp-formula><p>And more generally for isothermal transformation</p><disp-formula id="scirp.50604-formula1791"><label>(7)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x26.png"  xlink:type="simple"/></disp-formula><p>This cycle cannot work as a thermal engine.</p><p>The efficiency <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x27.png" xlink:type="simple"/></inline-formula> of the Carnot cycle is defined as the ratio of work supplied of the heat input, (i.e. by energy conservation), dividing heat balance by heat input:</p><disp-formula id="scirp.50604-formula1792"><label>(8)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x28.png"  xlink:type="simple"/></disp-formula><p>Hence [cf Equation (6)]</p><disp-formula id="scirp.50604-formula1793"><label>(9)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x29.png"  xlink:type="simple"/></disp-formula><p><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x30.png" xlink:type="simple"/></inline-formula>is not calculable. Rigorously, the Carnot efficiency (based on isothermal conditions) is not defined!</p></sec><sec id="s2_5"><title>2.5. Carnot Engine</title><p>The thermal cycle of a motor is traditionally represented as follows in <xref ref-type="fig" rid="fig5">Figure 5</xref>.</p><p>In motor mode, the heat from the hot source is partly converted in form of work, the balance going to the cold source.</p><p>And the thermal cycle of a refrigerating unit is traditionally represented as follows in <xref ref-type="fig" rid="fig6">Figure 6</xref>.</p><p>In refrigeration mode, the heat from the cold source goes to the hot source and the work too. How is it possible that the heat goes from cold to hot?</p><fig id="fig4"  position="float"><label><xref ref-type="fig" rid="fig4">Figure 4</xref></label><caption><title> Carnot cycle</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x31.png"/></fig><fig id="fig5"  position="float"><label><xref ref-type="fig" rid="fig5">Figure 5</xref></label><caption><title> Traditional representations of motor cycle</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x32.png"/></fig><fig id="fig6"  position="float"><label><xref ref-type="fig" rid="fig6">Figure 6</xref></label><caption><title> Traditional representations of cooling cycle</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x33.png"/></fig></sec></sec><sec id="s3"><title>3. Statement of Assumptions</title><p>The above points will be discussed again after the following assumptions:</p><sec id="s3_1"><title>3.1. Internal Energy U</title><p>Beforehand, what is the internal energy U? “The internal energy of given state cannot be directly measured. (∙∙∙) Though it is a macroscopic quantity, internal energy can be explained in microscopic terms by two theoretical virtual components. One is the microscopic kinetic energy (∙∙∙). The other is the potential energy (∙∙∙). There is no simple universal relation between these quantities of microscopic energy and the quantities of energy gained or lost by the system in work, heat, or matter transfer.” [<xref ref-type="bibr" rid="scirp.50604-ref12">12</xref>] . So the link between macroscopic and virtual microscopic components is:</p><disp-formula id="scirp.50604-formula1794"><label>(10)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x34.png"  xlink:type="simple"/></disp-formula><p>with E<sub>K</sub> for kinetic energy of particles and E<sub>P</sub> for potential energy</p><p>And the main property of U is: “The internal energy is a state function of the system, because its value depends only of the current state of the system and not on the path taken or processes undergone to prepare it.” [<xref ref-type="bibr" rid="scirp.50604-ref8">8</xref>] . This property does not change here.</p></sec><sec id="s3_2"><title>3.2. Emitted Heat Proportional to Temperature</title><p>The first new assumption is that all bodies emit heat, and this heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x35.png" xlink:type="simple"/></inline-formula> is proportional to the temperature T of the body over a period dt:</p><disp-formula id="scirp.50604-formula1795"><label>(11)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x36.png"  xlink:type="simple"/></disp-formula><p>with:</p><p>&#183; s coefficient, unit in [W/(K∙m<sup>2</sup>)]</p><p>&#183; A area of the body, in [m<sup>2</sup>]</p><p>&#183; T temperature of the body surface, in [K]</p><p>&#183; dt time length of the thermal exchange, in [s]</p><p>Remark: if entropy S in [J/K] has the properties of a status function, s is only a coefficient in [W/(K∙m<sup>2</sup>)]. And like C<sub>p</sub>, s is empirical and should be dependent for example on the temperature.</p></sec><sec id="s3_3"><title>3.3. Work of Internal Pressure</title><p>According to the fundamental principle of dynamics, acceleration undergone by a body is proportional to the net strength it received. The piston is moved because at a time that internal strength was different from the external strength, i.e. the internal pressure was different from the external pressure. See <xref ref-type="fig" rid="fig7">Figure 7</xref>.</p><p>It is considered here (please read arguments in Appendix) the internal strength or internal pressure, and therefore their work according to the formula:</p><disp-formula id="scirp.50604-formula1796"><label>(12)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x37.png"  xlink:type="simple"/></disp-formula><p>or</p><disp-formula id="scirp.50604-formula1797"><label>(13)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x38.png"  xlink:type="simple"/></disp-formula><p>Remark: The fundamental principle of dynamics indicates that if internal pressure equals constantly and exactly to external pressure, then there is no movement (for a body initially at rest): the reversible movement where constantly and exactly <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x39.png" xlink:type="simple"/></inline-formula> is impossible. The reversible movement is a limit but an unrealistic case.</p></sec><sec id="s3_4"><title>3.4. Variation of Internal Energy Function of Heat Transfer and Internal Pressure Work</title><p>The property to calculate the “variation” of U is traditionally given by <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x40.png" xlink:type="simple"/></inline-formula> [cf Equation (2)] with <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x40.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x41.png" xlink:type="simple"/></inline-formula> [cf Equation (4)] which gives.</p><fig id="fig7"  position="float"><label><xref ref-type="fig" rid="fig7">Figure 7</xref></label><caption><title> P<sub>int</sub> was different from P<sub>ext</sub></title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x42.png"/></fig><disp-formula id="scirp.50604-formula1798"><label>(14)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x43.png"  xlink:type="simple"/></disp-formula><p>Note than the variation of the “internal” energy would depend from the “external” pressure.</p><p>In this essay let us rather have the internal energy to depend from the internal pressure:</p><disp-formula id="scirp.50604-formula1799"><label>(15)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x44.png"  xlink:type="simple"/></disp-formula><p>or</p><disp-formula id="scirp.50604-formula1800"><label>(15bis)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x45.png"  xlink:type="simple"/></disp-formula><p>with <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x46.png" xlink:type="simple"/></inline-formula> [cf Equation (13)] which means</p><disp-formula id="scirp.50604-formula1801"><label>(16)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x47.png"  xlink:type="simple"/></disp-formula></sec><sec id="s3_5"><title>3.5. Comments</title><p>&#183; <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x48.png" xlink:type="simple"/></inline-formula>has only been changed into<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x48.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x49.png" xlink:type="simple"/></inline-formula>, there is no major change in the expression of <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x48.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x49.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x50.png" xlink:type="simple"/></inline-formula> and dU; no major change means that <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x48.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x49.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x50.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x51.png" xlink:type="simple"/></inline-formula> has in practice the same magnitude than <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x48.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x49.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x50.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x51.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x52.png" xlink:type="simple"/></inline-formula> (except of course in the particular case of expansion in vacuum).</p><p>&#183; When<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x53.png" xlink:type="simple"/></inline-formula>, then dU according to Equation (14) is equal to dU according to Equation (16):</p><disp-formula id="scirp.50604-formula1802"><label>(17)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x54.png"  xlink:type="simple"/></disp-formula><p>&#183; For reversible paths, <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x55.png" xlink:type="simple"/></inline-formula>, so there is no difference in the calculation of dU.</p><p>&#183; For irreversible paths, we will get a difference in the calculation of<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x56.png" xlink:type="simple"/></inline-formula>. This difference of work calculation will change the “predicted” reached point in the Clapeyron diagram; for example, shall we reach the temperature T<sub>1</sub> or T<sub>2</sub>? See <xref ref-type="fig" rid="fig8">Figure 8</xref>.</p><p>&#183; Then, to calculate the difference of internal energy from the initial point<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x57.png" xlink:type="simple"/></inline-formula>, we will choose a “reversible” path, and we have demonstrated herebefore there was no difference in the calculation of<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x57.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x58.png" xlink:type="simple"/></inline-formula>, and so in the calculation of the U status [we will find either <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x57.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x58.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x59.png" xlink:type="simple"/></inline-formula> or<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x57.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x58.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x59.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x60.png" xlink:type="simple"/></inline-formula>].</p><p>&#183; It confirms the U value of such defined point depends only of the current state of the system and not on the path taken or processes undergone to prepare it.</p><p>&#183; For ideal gas, the property that the macroscopic internal energy U depending only on the temperature (the Joule’s law) remains unchanged.</p><p>&#183; Due to Equation (10) and Equation (15bis), the link between the macroscopic value U and the virtual microscopic terms could be changed.</p><p>To sum up into a chart (Chart 1).</p></sec></sec><sec id="s4"><title>4. Consequences</title><p>In function of these hypotheses, points of Paragraph 2 are now discussed again.</p><fig id="fig8"  position="float"><label><xref ref-type="fig" rid="fig8">Figure 8</xref></label><caption><title> Change of the predicted reached point</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x61.png"/></fig><sec id="s4_1"><title>4.1. Thermal Balance and Heat Transfer</title><sec id="s4_1_1"><title>4.1.1. Concept</title><p>Suppose two identical bodies, except for temperature, in a fully insulated enclosure: all the heat emitted from one body A is received by the other body B (and vice versa). According to the first hypothesis of Equation (11) where <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x62.png" xlink:type="simple"/></inline-formula> is proportional to temperature, at every moment (see <xref ref-type="fig" rid="fig9">Figure 9</xref>):</p><p>&#183; the body A at the temperature T<sub>A</sub> emits the heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x63.png" xlink:type="simple"/></inline-formula> and receives from B the heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x63.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x64.png" xlink:type="simple"/></inline-formula></p><p>&#183; the body B at the temperature T<sub>B</sub> emits the heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x65.png" xlink:type="simple"/></inline-formula> and receives from A the heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x65.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x66.png" xlink:type="simple"/></inline-formula></p><p>&#183; For A, the balance between the emitted heat and the received heat is the heat<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x67.png" xlink:type="simple"/></inline-formula>:</p><disp-formula id="scirp.50604-formula1803"><label>(18)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x68.png"  xlink:type="simple"/></disp-formula><p>&#183; For B, the balance between the emitted heat and the received heat is the heat<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x69.png" xlink:type="simple"/></inline-formula>:</p><disp-formula id="scirp.50604-formula1804"><label>(19)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x70.png"  xlink:type="simple"/></disp-formula><p>This heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x71.png" xlink:type="simple"/></inline-formula> is nothing but the exchanged heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x71.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x72.png" xlink:type="simple"/></inline-formula> in the traditional theory.</p></sec><sec id="s4_1_2"><title>4.1.2. Generalization</title><p>&#183; We can note in the case of this single two bodies that</p><disp-formula id="scirp.50604-formula1805"><label>(20)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x73.png"  xlink:type="simple"/></disp-formula><p>This is in agreement with energy conservation, what is lost from one side is gained from the other side.</p><p>&#183; If for example<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x74.png" xlink:type="simple"/></inline-formula>, then according to Equation (11) on emitted heat</p><disp-formula id="scirp.50604-formula1806"><label>(21)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x75.png"  xlink:type="simple"/></disp-formula><p>and so</p><disp-formula id="scirp.50604-formula1807"><label>(22)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x76.png"  xlink:type="simple"/></disp-formula><p>The (hot) body A emits more heat than it receives.</p><p>By the same reasoning</p><p>Chart 1. Similarities and differences about internal energy.</p><fig id="fig9"  position="float"><label><xref ref-type="fig" rid="fig9">Figure 9</xref></label><caption><title> Heat transfer</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x84.png"/></fig><disp-formula id="scirp.50604-formula1808"><label>(23)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x85.png"  xlink:type="simple"/></disp-formula><p>The (cold) body B receives more heat than it emits.</p><p>Thus, the difference in heat is transferred from A to B, or in other words:</p><p>The heat “difference” goes from hot to cold.</p><p>Result: That prohibits the perpetual motion machine of the second kind where heat is directly removed from a body: for there to be heat transfer we need a heat differential that goes from hot to cold.</p></sec><sec id="s4_1_3"><title>4.1.3. Case of Equilibrium</title><p>When<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x86.png" xlink:type="simple"/></inline-formula>, then</p><disp-formula id="scirp.50604-formula1809"><label>(24)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x87.png"  xlink:type="simple"/></disp-formula><p>When heat balance is nil, the bodies remain in thermal equilibrium. But that does not mean the heat exchanged is non-existent, which means the exchange is balanced. That is why it is distinguished. So we will distinguish the “balance heat” <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x88.png" xlink:type="simple"/></inline-formula>from the “emitted heat”<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x88.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x89.png" xlink:type="simple"/></inline-formula>.</p><p>Using this argument on three bodies, mathematics proved that two temperatures equal to a third one are equal, and so the three bodies are in stable equilibrium; it would not be longer a thermodynamical principle, it would be a mathematical property.</p></sec><sec id="s4_1_4"><title>4.1.4. Extension</title><p>For radiative exchange, according to St&#233;fan-Boltzmann’s law, the emittance M of a black body is:</p><disp-formula id="scirp.50604-formula1810"><label>(25)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x90.png"  xlink:type="simple"/></disp-formula><p>with<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x91.png" xlink:type="simple"/></inline-formula>.</p><p>Let us have the hypothesis where the variable s would be equal to kT<sup>3</sup>:</p><disp-formula id="scirp.50604-formula1811"><label>(26)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x92.png"  xlink:type="simple"/></disp-formula><p>Note in this hypothesis the variable s increases as a function of temperature.</p><p>For a given area,</p><disp-formula id="scirp.50604-formula1812"><label>(27)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x93.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.50604-formula1813"><label>(28)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x94.png"  xlink:type="simple"/></disp-formula><p>For T<sub>A</sub> and T<sub>B</sub> of the same order of magnitude, let us have <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x95.png" xlink:type="simple"/></inline-formula> such as</p><disp-formula id="scirp.50604-formula1814"><label>, (29)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x96.png"  xlink:type="simple"/></disp-formula><p><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x97.png" xlink:type="simple"/></inline-formula>being small compared to T<sub>A</sub> and T<sub>B</sub>.</p><disp-formula id="scirp.50604-formula1815"><label>(30)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x98.png"  xlink:type="simple"/></disp-formula><p><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x99.png" xlink:type="simple"/></inline-formula>being small compared to T<sub>B</sub>,</p><disp-formula id="scirp.50604-formula1816"><label>(31)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x100.png"  xlink:type="simple"/></disp-formula><p>and with</p><disp-formula id="scirp.50604-formula1817"><label>(32)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x101.png"  xlink:type="simple"/></disp-formula><p>and <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x102.png" xlink:type="simple"/></inline-formula> according to Equation (23):</p><disp-formula id="scirp.50604-formula1818"><label>(33)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x103.png"  xlink:type="simple"/></disp-formula><p>On a low temperature range and for a given duration t, <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x104.png" xlink:type="simple"/></inline-formula>would be proportional to <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x104.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x105.png" xlink:type="simple"/></inline-formula> for radiative exchanges.</p></sec></sec><sec id="s4_2"><title>4.2. Joule Experiment and Adiabatic Expansion</title><sec id="s4_2_1"><title>4.2.1. The Joule’s Law and the Selected Experiments</title><p>First we have to distinguish</p><p>&#183; the Joule’s law: the internal energy depends only of the internal temperature for an ideal gas, from</p><p>&#183; the so-called experiment of Joule: the adiabatic expansion in vacuum. It is a specific experiment because it is done against vacuum, and so it is irreversible. Let us remind experiments and industrial practice indicate that without heat transfer <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x106.png" xlink:type="simple"/></inline-formula> the gases cool by relaxing (at temperatures lower than the Mariotte temperature and at low pressure).</p></sec><sec id="s4_2_2"><title>4.2.2. Usual Explanations</title><p>In the case of the expansion against vacuum, there is no heat exchange or external work exchange. Thus, according to Equation (14)<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x107.png" xlink:type="simple"/></inline-formula>, so U = Constant, and therefore (see Joule’s law) T = Constant. As this is in contradiction with the experimental results where the temperature is decreasing, it is said that the gases do not follow the ideal gas law [<xref ref-type="bibr" rid="scirp.50604-ref13">13</xref>] ! Equation (1) of ideal gas would be invalid in these cases. Why would not rather Equation (2) of internal energy and so Equation (14) be invalid for irreversible transformations? See <xref ref-type="fig" rid="fig1">Figure 1</xref>0 on incompatible assumptions.</p><p>Another explanation is to assert absolute vacuum does not exist (even in the intergalactic space, there is one particle per m<sup>3</sup>), there is always some molecules and thus a (tiny) level of external pressure<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x108.png" xlink:type="simple"/></inline-formula>, and therefore work of external forces:</p><disp-formula id="scirp.50604-formula1819"><label>(34)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x109.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.50604-formula1820"><label>(35)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x110.png"  xlink:type="simple"/></disp-formula><p>In this case, the gas should hardly cool (whereas in practice, the gas really cools).</p></sec><sec id="s4_2_3"><title>4.2.3. Proposed Explanation</title><p>According to Equation (16):<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x111.png" xlink:type="simple"/></inline-formula>. The internal pressure of the gas being never nil, the internal</p><fig id="fig10"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>0</label><caption><title> Incompatible assumptions</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x112.png"/></fig><p>work is not nil, <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x113.png" xlink:type="simple"/></inline-formula>, and<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x113.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x114.png" xlink:type="simple"/></inline-formula>, therefore<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x113.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x114.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x115.png" xlink:type="simple"/></inline-formula>: placing itself under the usual conditions (lower temperature than Mariotte temperature and so to a pressure where the molecules do not interact), the ideal gas must cool itself by relaxing in accordance with the present hypothesis, and in accordance with experiments (without making necessarily a perfect vacuum).</p><p>A more precise calculation will be to use the formula from the Appendix:</p><disp-formula id="scirp.50604-formula1821"><label>(36)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x116.png"  xlink:type="simple"/></disp-formula><p>Because <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x117.png" xlink:type="simple"/></inline-formula> and<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x117.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x118.png" xlink:type="simple"/></inline-formula>,</p><disp-formula id="scirp.50604-formula1822"><label>, (37)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x119.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.50604-formula1823"><label>. (38)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x120.png"  xlink:type="simple"/></disp-formula><p>The experimental results are in agreement with the Joule’s law: with the expansion work the temperature is decreasing; and so there is a loss of internal energy (gained by the expansion work).</p><p>Conversely, in case of compression, the temperature increases and the internal energy consequently.</p></sec></sec><sec id="s4_3"><title>4.3. The Area of Internal Pressure Work</title><p>During an expansion the volume increases, and so according to Equation (13) where<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x121.png" xlink:type="simple"/></inline-formula>: the internal work is positive<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x121.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x122.png" xlink:type="simple"/></inline-formula>.</p><p>When the abscise increases for a positive function, the mathematical integral represented by its area is positive<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x123.png" xlink:type="simple"/></inline-formula>. See <xref ref-type="fig" rid="fig1">Figure 1</xref>1.</p><p>The same reasoning can be applied to the volume restriction and to the negative integral.</p><p>There is total correlation between the thermo dynamical work of the internal pressure <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x124.png" xlink:type="simple"/></inline-formula> and the mathematical graphic representation <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x124.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x125.png" xlink:type="simple"/></inline-formula> in the Clapeyron diagram in [P-V].</p></sec><sec id="s4_4"><title>4.4. Engine Cycle</title><p>“A transformation is reversible if it can return to its initial position by a series of infinitesimal changes. It is only a thought experiment: the actual transformations are all irreversible” [<xref ref-type="bibr" rid="scirp.50604-ref14">14</xref>] .</p><p>The <xref ref-type="fig" rid="fig6">Figure 6</xref> represents the idealized but incorrect case where heat is transferred whereas the internal fluid is at the same temperature as the hot source, and then at the same temperature as the cold source. For there to be heat transfer, “in practice, there must be some difference in temperature between the machine and the hot and cold sources” [<xref ref-type="bibr" rid="scirp.50604-ref15">15</xref>] . For the refrigerating machine, the fluid must be compressed to a temperature above the hot source, and then expanded to a temperature below the cold source for it to work. The <xref ref-type="fig" rid="fig6">Figure 6</xref> should be reviewed as follows in <xref ref-type="fig" rid="fig1">Figure 1</xref>2.</p><p>In refrigeration mode, heat of the cold source goes towards the colder fluid. Then the cycle fluid is compressed by the work done up to a temperature above the heat source for the heat dissipation of the fluid. And to close the cycle, the fluid is relaxed and cooled itself to return to the initial conditions.</p><fig id="fig11"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>1</label><caption><title> Representation of internal pressure work</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x126.png"/></fig><p>The <xref ref-type="fig" rid="fig5">Figure 5</xref> of the motor cycle are also idealized and incorrect, as there is no transfer of heat if the fluid is at the same temperature as the hot source, and then as the cold source. The <xref ref-type="fig" rid="fig5">Figure 5</xref> should be reviewed as follows in <xref ref-type="fig" rid="fig1">Figure 1</xref>3.</p><p>In motor mode, heat from the heat source goes to the cooler fluid, the fluid expansion provides work (and to complete the cycle, the fluid transfers the heat balance to the cold source).</p></sec><sec id="s4_5"><title>4.5. Motor Efficiency</title><sec id="s4_5_1"><title>4.5.1. Motor Efficiency Formula</title><p>And <xref ref-type="fig" rid="fig4">Figure 4</xref> would have to be reviewed as follows in <xref ref-type="fig" rid="fig1">Figure 1</xref>4.</p><fig id="fig12"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>2</label><caption><title> Proposed representation of cooling cycle</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x127.png"/></fig><fig id="fig13"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>3</label><caption><title> Proposed representation of motor cycle</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x128.png"/></fig><fig id="fig14"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>4</label><caption><title> Proposed Carnot engine</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x129.png"/></fig><p>If this cycle is more realistic, it will generate complicated equations to calculate variable temperatures. That is why it is suggested here the following simplification, knowing that t<sub>H</sub> and t<sub>C</sub> are approximately (not exactly) constant. Let us characterize it with equations:</p><p>The heat transferred to the (relative) hot fluid from the Hot source is (cf Equations (11) and (18)):</p><disp-formula id="scirp.50604-formula1824"><label>(39)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x130.png"  xlink:type="simple"/></disp-formula><p>Note: the Hot source and the (relative) hot fluid being substantially at the same temperature, we consider firstly that they have substantially the same s<sub>H</sub> (idem for s<sub>C</sub>).</p><p>For writing formulas reason, let us simplify the expression: <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x131.png" xlink:type="simple"/></inline-formula>into Q<sub>H</sub> (and <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x131.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x132.png" xlink:type="simple"/></inline-formula> into Q<sub>C</sub>).</p><disp-formula id="scirp.50604-formula1825"><label>(40)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x133.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.50604-formula1826"><label>(41)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x134.png"  xlink:type="simple"/></disp-formula><p>And the heat transferred from the (relative) cold fluid to the Cold source is [cf Equation (11) and Equation (19)]:</p><disp-formula id="scirp.50604-formula1827"><label>(42)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x135.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.50604-formula1828"><label>(43)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x136.png"  xlink:type="simple"/></disp-formula><p>Preliminary remark: according that we adhere or not to the hypothesis expressed by Equation (15) taking into account internal work, demonstration hereafter does not change, it is why it is denoted by<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x137.png" xlink:type="simple"/></inline-formula>, which can represent as well <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x137.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x138.png" xlink:type="simple"/></inline-formula> as<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x137.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x138.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x139.png" xlink:type="simple"/></inline-formula>.</p><p>For a motor cycle:</p><disp-formula id="scirp.50604-formula1829"><label>(44)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x140.png"  xlink:type="simple"/></disp-formula><p>Motor efficiency <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x141.png" xlink:type="simple"/></inline-formula> is:</p><disp-formula id="scirp.50604-formula1830"><label>(45)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x142.png"  xlink:type="simple"/></disp-formula><p>or according to Equation (44):</p><disp-formula id="scirp.50604-formula1831"><label>(46)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x143.png"  xlink:type="simple"/></disp-formula><p>and using equalities (40) and (42):</p><disp-formula id="scirp.50604-formula1832"><label>(47)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x144.png"  xlink:type="simple"/></disp-formula><p>On the same range of temperature, <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x145.png" xlink:type="simple"/></inline-formula>, so</p><disp-formula id="scirp.50604-formula1833"><label>(48)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x146.png"  xlink:type="simple"/></disp-formula><p>which, for effective engine, is more accurate than the usual limit inequality <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x147.png" xlink:type="simple"/></inline-formula> [cf Equation (5)].</p></sec><sec id="s4_5_2"><title>4.5.2. Theoretical Example</title><p>To get a better understanding, let us apply to a theoretical example, the irreversible Carnot engine, as described in <xref ref-type="fig" rid="fig1">Figure 1</xref>5.</p><p>The effective efficiency is according to definition Equation (45):</p><disp-formula id="scirp.50604-formula1834"><label>(49)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x148.png"  xlink:type="simple"/></disp-formula><fig id="fig15"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>5</label><caption><title> Irreversible Carnot engine</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x149.png"/></fig><p>If we use the efficiency of irreversible cycle based on temperatures as seen Equation (48):</p><disp-formula id="scirp.50604-formula1835"><label>(50)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x150.png"  xlink:type="simple"/></disp-formula><p>which has the same value than the effective efficiency,.</p><p>Thus the Carnot efficiency based on sources temperatures is, according to Equation (5):</p><disp-formula id="scirp.50604-formula1836"><label>(51)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x151.png"  xlink:type="simple"/></disp-formula><p>which is slightly higher than the effective efficiency.</p><p>We can of course find the efficiency of 60% if we consider the cycle temperatures instead of the sources temperatures. The trouble is Carnot “engine” with isothermal evolution is unrealistic as explained &#167;2.4. So, let us check another simple example.</p></sec><sec id="s4_5_3"><title>4.5.3. Application</title><p>Then we will apply this property of the efficiency to a non-biphasic cycle: the very simple but more realistic elevator engine given by Pr. Richard Taillet [<xref ref-type="bibr" rid="scirp.50604-ref16">16</xref>] . <xref ref-type="fig" rid="fig1">Figure 1</xref>6 and Chart 2 sum up the results:</p><p>In this non-biphasic cycle, the net work is −45 kJ for a heat transfer of (122 + 868 =) 990 kJ. The cycle effective efficiency is very low, (45/990 =) 5%.</p><p>When we apply the Carnot efficiency, with a 746 K hot temperature and a 300 K cold temperature, the maximum efficiency is according to Equation (5):</p><disp-formula id="scirp.50604-formula1837"><label>(52)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x152.png"  xlink:type="simple"/></disp-formula><p>The maximum efficiency (60%) based on sources temperatures is very far of this cycle efficiency (5%).</p><p>To apply the new efficiency formula, we strictly should have used the instantaneous temperatures and integrate them, which would be very difficult here. So, only to give an order of magnitude, we will take in this example an average temperature of ((373 + 746)/2 =) 560 K for the hot side, and an average temperature of ((600 + 300)/2 =) 450 K for the cold side. An irreversible efficiency should be closed to</p><disp-formula id="scirp.50604-formula1838"><label>(53)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x153.png"  xlink:type="simple"/></disp-formula><p>An irreversible efficiency (19%) based on differences of temperatures is closer to the effective efficiency (5%).</p><p>Previous calculation (19%) was done with a very approximative but simple average temperature only to explain. It has also been taken final fluid temperatures equal to the source temperature, which would mean a perfect heat exchanger. In practice, we will get for example 4 to 5 K between the final fluid temperature and the</p><fig id="fig16"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>6</label><caption><title> Non-biphasic motor cycle</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x154.png"/></fig><p>Chart 2. Cycle results.</p><p>source temperature:<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x155.png" xlink:type="simple"/></inline-formula>. Let us use the more accurate logarithmic difference of temperature <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x155.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x156.png" xlink:type="simple"/></inline-formula> used with heat exchangers:</p><disp-formula id="scirp.50604-formula1839"><label>(54)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x157.png"  xlink:type="simple"/></disp-formula><p>which would give</p><disp-formula id="scirp.50604-formula1840"><label>(55)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x158.png"  xlink:type="simple"/></disp-formula><p>and, because <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x159.png" xlink:type="simple"/></inline-formula> is in practice a bit lower on the cold side than on the hot side</p><disp-formula id="scirp.50604-formula1841"><label>(56)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x160.png"  xlink:type="simple"/></disp-formula><p>so</p><disp-formula id="scirp.50604-formula1842"><label>(57)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x161.png"  xlink:type="simple"/></disp-formula><p>which is in good correlation with the 5% of the effective efficiency.</p></sec></sec></sec><sec id="s5"><title>5. Conclusion and Summary</title><p>Slightly modifying the concepts of heat transfer and work, we have given different explanations, and hopefully clearer on:</p><p>&#183; the thermal balance and the heat transfer direction;</p><p>&#183; the effects of expansion in the so-called experiments of Joule;</p><p>&#183; the direct reading of the work in the Clapeyron diagram;</p><p>Chart 3. Comparison chart.</p><p>&#183; a more accurate use of diagram of thermal cycles, especially for irreversible transformations in the motor cycle and the refrigeration cycle;</p><p>&#183; a new property for irreversible engine efficiency:<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x186.png" xlink:type="simple"/></inline-formula>.</p><p>You will find a chart (Chart 3) to sum up the proposed formulas vs. the traditional formulas.</p><p>Without questioning the experimental results and the reversible predictions, the purpose of this essay is contributing to evolve the presentation of the thermodynamics traditional explanations, taking better account of Irreversibility.</p></sec><sec id="s6"><title>Acknowledgements</title><p>I would like to thank Daniel Mandineau for his teaching of traditional thermodynamics.</p></sec><sec id="s7"><title>Appendix</title>Arguments for Internal Pressure Work<p>1) Work of external pressure</p><p>Because<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x187.png" xlink:type="simple"/></inline-formula>,</p><disp-formula id="scirp.50604-formula1843"><label>(A.1)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x188.png"  xlink:type="simple"/></disp-formula><p>this means <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x189.png" xlink:type="simple"/></inline-formula> is nothing but the work supplied (or received) by the outside to the (internal) system.</p><p>b) Work of internal pressure</p><p>More than the work supplied by the external, it would be more rigorous to take in count the work received (or supplied) by the (internal) system:<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x190.png" xlink:type="simple"/></inline-formula>.</p><p>Due to the conservation of energy, the trouble is why the supplied work <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x191.png" xlink:type="simple"/></inline-formula> would not be equal to the received work<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x191.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x192.png" xlink:type="simple"/></inline-formula>? See <xref ref-type="fig" rid="fig1">Figure 1</xref>7.</p><p>To get a movement, it is necessary to have<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x193.png" xlink:type="simple"/></inline-formula>, so<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x193.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x194.png" xlink:type="simple"/></inline-formula>.</p><p>3) Effective work</p><p>Effective work, supplied and received, is in fact</p><disp-formula id="scirp.50604-formula1844"><label>(A.2)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x195.png"  xlink:type="simple"/></disp-formula><p>this will be difficult to integrate</p><disp-formula id="scirp.50604-formula1845"><label>(A.3)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x196.png"  xlink:type="simple"/></disp-formula><p>So previous equation can be approximated by</p><fig id="fig17"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>7</label><caption><title> W<sub>ext</sub> and W<sub>int</sub></title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x197.png"/></fig><fig id="fig18"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref>8</label><caption><title> Effective work (supplied and received)</title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/4-7501964x198.png"/></fig><disp-formula id="scirp.50604-formula1846"><label>(A.4)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/4-7501964x199.png"  xlink:type="simple"/></disp-formula><p>See <xref ref-type="fig" rid="fig1">Figure 1</xref>8.</p><p>For pragmatic reasons (for example Clapeyron diagram, cf &#167;4.3), it has been chosen here to represent <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x200.png" xlink:type="simple"/></inline-formula> by<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x200.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/4-7501964x201.png" xlink:type="simple"/></inline-formula>, but if high precision is required, one of the two previous formulas [(A.4) or more precisely (A.2)] will be necessary.</p></sec></body><back><ref-list><title>References</title><ref id="scirp.50604-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Balian, R., CEA (2013) La longue elaboration du concept d'energie. http://www.academie-sciences.fr/activite/hds/textes/evol_Balian1.pdf</mixed-citation></ref><ref id="scirp.50604-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Diu, B. 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