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		<id>https://en.formulasearchengine.com/index.php?title=Inductive_effect&amp;diff=11325</id>
		<title>Inductive effect</title>
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		<updated>2013-10-22T14:20:52Z</updated>

		<summary type="html">&lt;p&gt;164.111.235.237: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;The &#039;&#039;&#039;Benedict–Webb–Rubin equation&#039;&#039;&#039; (&#039;&#039;&#039;BWR&#039;&#039;&#039;), named after [[Manson Benedict]], G. B. Webb, and L. C. Rubin, is an [[equation of state]] used in [[fluid dynamics]].   Working at the research laboratory of [[M. W. Kellogg Limited]], the three researchers rearranged the [[Beattie–Bridgeman model|Beattie-Bridgeman Equation of State]] and increased the number of experimentally determined constants to eight.&amp;lt;ref name=bwr1940&amp;gt;{{citation|last1=Benedict|first1=Manson|last2=Webb|first2=George B.|last3=Rubin|first3=Louis C.|title=An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures: I. Methane, Ethane, Propane, and n-Butane|journal=[[Journal of Chemical Physics]]|volume= 8|number=4|page= 334&amp;amp;ndash;345|year=1940|issn=0021-9606|doi=10.1063/1.1750658|bibcode = 1940JChPh...8..334B }}&amp;lt;/ref&amp;gt;&amp;lt;ref&amp;gt;{{citation|url=http://www.ecourses.ou.edu/cgi-bin/ebook.cgi?doc=&amp;amp;topic=th&amp;amp;chap_sec=02.4&amp;amp;page=theory|contribution=The Ideal-gas Equation of State|title=Multimedia Engineering Thermodynamics|last2=Huang|first2=Meirong |first1=Kurt|last2= Gramoll|accessdate=May 16, 2012}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==The original BWR equation==&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;P=\rho RT + \left(B_0 RT-A_0 - \frac{C_0}{T^2} \right) \rho^2 + \left(bRT-a\right) \rho^3 + \alpha  a  \rho^6 + \frac{c\rho^3}{T^2}\left(1 + \gamma\rho^2\right)\exp\left(-\gamma\rho^2\right)&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==The BWRS equation of state==&lt;br /&gt;
&lt;br /&gt;
A modification of the Benedict–Webb–Rubin equation of state by Professor Kenneth E. Starling of the University of Oklahoma:&amp;lt;ref name=starling&amp;gt;{{citation|title=Fluid Properties for Light Petroleum Systems|last=Starling|first=Kenneth E.|publisher=Gulf Publishing Company|year=1973|isbn=978-0872012936|pages=270}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;P=\rho RT + \left(B_0 RT-A_0 - \frac{C_0}{T^2} + \frac{D_0}{T^3} - \frac{E_0}{T^4}\right) \rho^2 + \left(bRT-a-\frac{d}{T}\right) \rho^3 + \alpha\left(a+\frac{d}{T}\right) \rho^6 + \frac{c\rho^3}{T^2}\left(1 + \gamma\rho^2\right)\exp\left(-\gamma\rho^2\right)&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&#039;&#039;&amp;amp;rho;&#039;&#039; = the [[molar density]].&lt;br /&gt;
&lt;br /&gt;
Values of the various parameters for 15 substances can be found in Starling&#039;s &#039;&#039;Fluid Properties for Light Petroleum Systems.&#039;&#039;.&amp;lt;ref name=starling/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==The Modified BWR equation (mBWR){{anchor|mbwr}}==&lt;br /&gt;
&lt;br /&gt;
A further modification of the Benedict–Webb–Rubin equation of state by Jacobsen and Stewart:&amp;lt;ref name=jacobsen&amp;gt;{{citation|first1=Robert C. |last1=Reid|first2=John M.|last2= Prausnitz|first3=Bruce E.|last3=Poling|title=The Properties of Gases &amp;amp; Liquids| edition=4th |publisher=McGraw-Hill|location=New York|date=April 1987|isbn=978-0070517998|pages=741}}&lt;br /&gt;
*{{citation|first1=Richard T. |last=Jacobsen|first2=Richard B.|last2=Stewart|title=Thermodynamic Properties of Nitrogen Including Liquid and Vapor Phases from 63 K to 2000 K with Pressures to 10,000 Bar|journal= Journal of Physical and Chemical Reference Data|doi=10.1063/1.555785|volume=2|number=4|page=757&amp;amp;ndash;922 |year=1973|publisher=[[National Institute of Standards and Technology]]|url=http://www.nist.gov/data/PDFfiles/jpcrd39.pdf|format=pdf|issn=0047-2689|doi=10.1063/1.3253132|bibcode = 1973JPCRD...2..757J }}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;P=\sum_{n=1}^{9}a_n\rho^n+\exp\left(-\gamma\rho^2\right)\sum_{n=10}^{15}a_n\rho^{2n-17}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
:&amp;lt;math&amp;gt;\gamma=1/\rho_c^2&amp;lt;/math&amp;gt;&lt;br /&gt;
&amp;lt;br&amp;gt;&lt;br /&gt;
The mBWR equation subsequently evolved into a 32 term version (Younglove and Ely, 1987) with numerical parameters determined by fitting the equation to empirical data for a reference fluid.&amp;lt;ref name=younglove&amp;gt;{{citation|last1=Younglove|first1=B. A.|first2= J. F. |last2=Ely|title=Thermophysical Properties of Fluids II Methane, Ethane, Propane, Isobutane, and Normal Butane|journal= Journal of Physical and Chemical Reference Data|issn=0047-2689|doi=10.1063/1.555785|volume=16|page=577|year=1987}}&amp;lt;/ref&amp;gt;  Other fluids then are described by using reduced variables for temperature and density.&amp;lt;ref&amp;gt;{{citation|url=http://repository.tamu.edu/bitstream/handle/1969.1/1094/etd-tamu-2003B-2003062110-Widi-1.pdf|page=11|title=Variation of Density with Composition for Natural Gas Mixtures in the Supercritical Region |date=August 2003|last=Widia|first=B. S.|format=thesis|publisher=[[Texas A&amp;amp;M University]]}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==See also==&lt;br /&gt;
* [[Real gas]]&lt;br /&gt;
&lt;br /&gt;
==References==&lt;br /&gt;
{{reflist}}&lt;br /&gt;
&lt;br /&gt;
==Further reading==&lt;br /&gt;
&lt;br /&gt;
*{{citation|last1=Benedict|first1=Manson|author1-link=Manson Benedict|last2=Webb|first2=George B.|last3=Rubin|first3=Louis C.|title=Mixtures of Methane, Ethane, Propane and &#039;&#039;n&#039;&#039;-Butane|journal=[[Journal of Chemical Physics]]|volume= 10|number=12|page= 747&amp;amp;ndash;758|year=1942|issn=0021-9606|doi=10.1063/1.1723658|bibcode = 1942JChPh..10..747B }}&lt;br /&gt;
*{{citation|last1=Benedict|first1=Manson|last2=Webb|first2=George B.|last3=Rubin|first3=Louis C.|title=An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures. &#039;&#039;&#039;Constants for Twelve Hydrocarbons&#039;&#039;&#039;| journal=Chemical Engineering Progress (CEP)|volume=47|number=8|page= 419&amp;amp;ndash;422 |year=1951}}&lt;br /&gt;
*{{citation|last1=Benedict|first1=Manson|last2=Webb|first2=George B.|last3=Rubin|first3=Louis C.|title=An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures &#039;&#039;&#039;Fugacities and Liquid-Vapor Equilibria&#039;&#039;&#039;| journal=Chemical Engineering Progress (CEP)|volume=47|number=9|page= 449&amp;amp;ndash;454 |year=1951}}.&lt;br /&gt;
&lt;br /&gt;
{{DEFAULTSORT:Benedict-Webb-Rubin equation}}&lt;br /&gt;
[[Category:Equations of fluid dynamics]]&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
{{fluiddynamics-stub}}&lt;/div&gt;</summary>
		<author><name>164.111.235.237</name></author>
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