<?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.2017.85052</article-id><article-id pub-id-type="publisher-id">JMP-75832</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>
 
 
  On Nernst’s Theorem and Compressibilities
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>James</surname><given-names>R. McNabb III</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Shigeji</surname><given-names>Fujita</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Akira</surname><given-names>Suzuki</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>Department of Physics, University at Buffalo, SUNY, Buffalo, USA</addr-line></aff><aff id="aff2"><addr-line>Department of Physics, Tokyo University of Science, Tokyo, Japan</addr-line></aff><pub-date pub-type="epub"><day>17</day><month>04</month><year>2017</year></pub-date><volume>08</volume><issue>05</issue><fpage>839</fpage><lpage>843</lpage><history><date date-type="received"><day>March</day>	<month>14,</month>	<year>2017</year></date><date date-type="rev-recd"><day>Accepted:</day>	<month>April</month>	<year>25,</year>	</date><date date-type="accepted"><day>April</day>	<month>30,</month>	<year>2017</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 unattainability of the absolute zero of temperature is proved by using Carnot’s theorem. Hence this unattainability is distinct from the Planck-Fer-mi statement of the Third Law of Thermodynamics that the entropy vanishes at  
  <em>T</em>=0. It is shown that the isothermal compressibility 
  <em>K</em>
  <sub>T</sub> is in general larger than the adiabatic compressibility 
  <em>K</em>
  <sub>s</sub> and the difference 
  <em style="white-space:normal;">K</em>
  <sub style="white-space:normal;">T </sub>
  &amp;minus; 
  <em style="white-space:normal;">K</em>
  <sub style="white-space:normal;">s </sub>vanishes in the low temperature limit.
 
</p></abstract><kwd-group><kwd>Nernst’s Theorem</kwd><kwd> Carnot’s Theorem</kwd><kwd> Adiabatic Compressibility</kwd><kwd> Isothermal  Compressibility: The Third Law of Thermodynamics</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Fermi in his book [<xref ref-type="bibr" rid="scirp.75832-ref1">1</xref>] stated for the Third Law that the entropy S of any system approaches zero in the zero temperature limit:</p><disp-formula id="scirp.75832-formula452"><label>(1)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x6.png"  xlink:type="simple"/></disp-formula><p>This form was proposed earlier by Planck, and will be called Planck-Fermi’s statement. Reif in his book [<xref ref-type="bibr" rid="scirp.75832-ref2">2</xref>] took a view that thermodynamics and statistical mechanics should be studied jointly by introducing Boltzmann’s connection between the entropy S and the number of microstates <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x7.png" xlink:type="simple"/></inline-formula> compatible with a set of macroscopic descriptors E, V, and N:</p><disp-formula id="scirp.75832-formula453"><label>(2)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x8.png"  xlink:type="simple"/></disp-formula><p>Nernst’s theorem (the third law) was expressed as</p><disp-formula id="scirp.75832-formula454"><label>(3)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x9.png"  xlink:type="simple"/></disp-formula><p>The difference between the two statements is due to the zero point motion arising from the Heisenberg’s uncertainty principle. Neither disorder nor dissipation can be generated by the zero-point motion. Quantum statistics will play a roll.</p><p>Pauli, in his book [<xref ref-type="bibr" rid="scirp.75832-ref3">3</xref>] , showed that the unattainability of absolute zero can be derived from Planck-Fermi’s statement by considering Carnot’s cycles. We shall show in the present work that the unattainability can be derived by using Carnot’s theorem (the second law).</p><p>The heat absorbed by a body is denoted by Q. The heat capacity C is defined by</p><disp-formula id="scirp.75832-formula455"><label>(4)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x10.png"  xlink:type="simple"/></disp-formula><p>This molar heat at constant volume, <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x11.png" xlink:type="simple"/></inline-formula>, and that at constant pressure, <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x12.png" xlink:type="simple"/></inline-formula>, are defined by</p><disp-formula id="scirp.75832-formula456"><label>(5)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x13.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.75832-formula457"><label>(6)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x14.png"  xlink:type="simple"/></disp-formula><p>where E and <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x15.png" xlink:type="simple"/></inline-formula> are the internal energy and the enthalpy, respectively. We assume that all thermodynamic functions for a one-component system are analytic within each domain of the gas, liquid and solid (phases). The thermodynamic functions are singular on the phase boundary. The body temperature should rise when heat is supplied. Hence the heat capacity should be non-negative. The body volume should become smaller when a pressure is applied from outside. Hence the compressibility should be positive.</p><p>Pauli showed in his book [<xref ref-type="bibr" rid="scirp.75832-ref3">3</xref>] that</p><disp-formula id="scirp.75832-formula458"><label>(7)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x16.png"  xlink:type="simple"/></disp-formula><p>by using the increasing entropy principle. The difference between <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x17.png" xlink:type="simple"/></inline-formula> and <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x18.png" xlink:type="simple"/></inline-formula> is given by</p><disp-formula id="scirp.75832-formula459"><label>(8)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x19.png"  xlink:type="simple"/></disp-formula><p>where</p><disp-formula id="scirp.75832-formula460"><label>(9)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x20.png"  xlink:type="simple"/></disp-formula><p>is the coefficient of thermal expansion and</p><disp-formula id="scirp.75832-formula461"><label>(10)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x21.png"  xlink:type="simple"/></disp-formula><p>is the isothermal compressibility.</p><p>We see from Equation (8),</p><disp-formula id="scirp.75832-formula462"><label>(11)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x22.png"  xlink:type="simple"/></disp-formula><p>The adiabatic compressibility <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x23.png" xlink:type="simple"/></inline-formula> is defined by</p><disp-formula id="scirp.75832-formula463"><label>(12)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x24.png"  xlink:type="simple"/></disp-formula><p>Both <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x25.png" xlink:type="simple"/></inline-formula> and <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x25.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x26.png" xlink:type="simple"/></inline-formula> are positive. Since the restoring forces are different the compressibility <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x25.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x26.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x27.png" xlink:type="simple"/></inline-formula> are distinct in the different phases.</p><p>We shall show newly in Section 3 that</p><disp-formula id="scirp.75832-formula464"><label>(13)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x28.png"  xlink:type="simple"/></disp-formula></sec><sec id="s2"><title>2. The Unattainnability of the Absolute Zero</title><p>Let us consider a gas. In the Carnot cycle shown in <xref ref-type="fig" rid="fig1">Figure 1</xref> the heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x29.png" xlink:type="simple"/></inline-formula> are absorbed (emmitted) on isothermal lines AB (CD) and the cycle is closed on adiabatic lines BC (DA). Carnot’s equation is given by</p><disp-formula id="scirp.75832-formula465"><label>(14)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x30.png"  xlink:type="simple"/></disp-formula><p>The efficiency of the Carnot’s engine is</p><disp-formula id="scirp.75832-formula466"><label>(15)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x31.png"  xlink:type="simple"/></disp-formula><p>where W is the work produced. According to Carnot’s theorem, no engine working between two temperatures <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x32.png" xlink:type="simple"/></inline-formula> can have a hgher efficiency than the Carnot engine. Thus the Carnot efficiency <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x32.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x33.png" xlink:type="simple"/></inline-formula> represents the highest possible efficiency for any engine working between <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x32.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x33.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x34.png" xlink:type="simple"/></inline-formula> and<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x32.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x33.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x34.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x35.png" xlink:type="simple"/></inline-formula>,<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x32.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x33.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x34.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x35.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x36.png" xlink:type="simple"/></inline-formula>.</p><p>In the Carnot cycle operated in the reverse direction an amount of heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x37.png" xlink:type="simple"/></inline-formula> is extracted from the low temperature reservoir. We may look at it as an ideal refrigirator if we regard the high temperature <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x37.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x38.png" xlink:type="simple"/></inline-formula> as the environment temperature. By solving Carnot’s equations Equations (14) and (15) we obtain</p><disp-formula id="scirp.75832-formula467"><label>(16)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x39.png"  xlink:type="simple"/></disp-formula><p>This expression indicates that the work W needed to extract a fixed amount of heat <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x40.png" xlink:type="simple"/></inline-formula> from a body at <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x40.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x41.png" xlink:type="simple"/></inline-formula> becomes greater as <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x40.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x41.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x42.png" xlink:type="simple"/></inline-formula> decreases. Accordingly, the operating cost of a refrigerator is higher if the temperature is set lower. Furthermore, if the temperature <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x40.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x41.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x42.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x43.png" xlink:type="simple"/></inline-formula> were to approach absolute zero, the work W needed will approach infinity. This means that attaining absolute zero by any means is impossible. All actual refrigerating machines must involve irreversible</p><fig id="fig1"  position="float"><label><xref ref-type="fig" rid="fig1">Figure 1</xref></label><caption><title> The Carnot (ideal) cycle: P-V Diagram and a schematic of a Carnot engine operating between hot and cold reservoirs at temperatures <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x45.png" xlink:type="simple"/></inline-formula> and<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x45.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x46.png" xlink:type="simple"/></inline-formula></title></caption><graphic mimetype="image"   position="float"  xlink:type="simple"  xlink:href="http://html.scirp.org/file/7-7503114x44.png"/></fig><p>processes which add an extra heat to the right-hand side of Equation (16).</p></sec><sec id="s3"><title>3. Isothermal and Adiabatic Compressibilities Approach Each Other in the Low Temperature Limit</title><p>After straightforward calculations which are outlined in Appendix, we obtain</p><disp-formula id="scirp.75832-formula468"><label>(17)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x47.png"  xlink:type="simple"/></disp-formula><p>Using this we obtain</p><disp-formula id="scirp.75832-formula469"><label>(18)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x48.png"  xlink:type="simple"/></disp-formula><p>The last inequality follows from inequalities in Equation (8). Hence the iso- thermal compressibility <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x49.png" xlink:type="simple"/></inline-formula> is in general larger than the adiabatic compressi- bility<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x49.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x50.png" xlink:type="simple"/></inline-formula>. Using Equation (11), we then obtain</p><disp-formula id="scirp.75832-formula470"><label>(19)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x51.png"  xlink:type="simple"/></disp-formula></sec><sec id="s4"><title>Cite this paper</title><p>McNabb III, J.R., Fujita, S. and Suzuki, A. (2017) On Nernst’s Theorem and Compressibilities. Journal of Modern Physics, 8, 839-843. https://doi.org/10.4236/jmp.2017.85052</p></sec><sec id="s5"><title>Appendix: Derivation of Equation (17)</title><p>Pressure P, volume V and temperature T are interrelated by the equation of state. If the variables <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x52.png" xlink:type="simple"/></inline-formula> are interrelated, then the differentials are related as</p><disp-formula id="scirp.75832-formula471"><label>(20)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x53.png"  xlink:type="simple"/></disp-formula><p>From this we obtain</p><disp-formula id="scirp.75832-formula472"><label>(21)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x54.png"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.75832-formula473"><label>(22)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x55.png"  xlink:type="simple"/></disp-formula><p>Using Equations (12) and (22), we obtain</p><disp-formula id="scirp.75832-formula474"><label>(23)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x56.png"  xlink:type="simple"/></disp-formula><p>If we regard S as a function of <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x57.png" xlink:type="simple"/></inline-formula> and T as a function of<inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x57.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x58.png" xlink:type="simple"/></inline-formula>:</p><p><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x59.png" xlink:type="simple"/></inline-formula>, <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x59.png" xlink:type="simple"/></inline-formula><inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x60.png" xlink:type="simple"/></inline-formula>we get</p><disp-formula id="scirp.75832-formula475"><label>(24)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x61.png"  xlink:type="simple"/></disp-formula><p>Similarly, we obtain</p><disp-formula id="scirp.75832-formula476"><label>(25)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x62.png"  xlink:type="simple"/></disp-formula><p>Using Equations (10), (23)-(25), we obtain</p><disp-formula id="scirp.75832-formula477"><label>(26)</label><graphic position="anchor" xlink:href="http://html.scirp.org/file/7-7503114x63.png"  xlink:type="simple"/></disp-formula><p>Dividing this by <inline-formula><inline-graphic xlink:href="http://html.scirp.org/file/7-7503114x64.png" xlink:type="simple"/></inline-formula> we obtain Equation (17).</p></sec></body><back><ref-list><title>References</title><ref id="scirp.75832-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Fermi, E. (1957) Thermodynamics. Dover, New York, 139.</mixed-citation></ref><ref id="scirp.75832-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Reif, F. (1965) Fundamentals of Statistical and Thermal Physics. McGraw Hill, New York, 122-123.</mixed-citation></ref><ref id="scirp.75832-ref3"><label>3</label><mixed-citation publication-type="other" xlink:type="simple">Pauli, W. (1973) Thermodynamics and the Kinetic Theory of Gasses. Dover, Mincola, New York, 83-86, 92-93.</mixed-citation></ref></ref-list></back></article>