theorem of corresponding states

{{Thermodynamics|cTopic=System properties}}

According to van der Waals, the theorem of corresponding states (or principle/law of corresponding states) indicates that all fluids, when compared at the same reduced temperature and reduced pressure, have approximately the same compressibility factor and all deviate from ideal gas behavior to about the same degree.{{cite book |author1=Tester, Jefferson W. |author2=Modell, Michael |name-list-style=amp |title=Thermodynamics and its applications |publisher=Prentice Hall |year=1997 |isbn=0-13-915356-X}}{{cite book|author1=Çengel Y.A. |author2=Boles M.A. |title=Thermodynamics: An Engineering Approach|edition=Sixth|publisher=McGraw Hill|year= 2007|isbn=9780071257718}} page 141

Material constants that vary for each type of material are eliminated, in a recast reduced form of a constitutive equation. The reduced variables are defined in terms of critical variables.

The principle originated with the work of Johannes Diderik van der Waals in about 1873[http://digital.library.okstate.edu/oas/oas_pdf/v56/p125_132.pdf A Four-Parameter Corresponding States Correlation for Fluid Compressibility Factors] {{Webarchive|url=https://web.archive.org/web/20070317215431/http://digital.library.okstate.edu/oas/oas_pdf/v56/p125_132.pdf |date=2007-03-17 }} by Walter M. Kalback and Kenneth E. Starling, Chemical Engineering Department, University of Oklahoma. when he used the critical temperature and critical pressure to derive a universal property of all fluids that follow the van der Waals equation of state. It predicts a value of 3/8 = 0.375 that is found to be an overestimate when compared to real gases.

Edward A. Guggenheim used the phrase "Principle of Corresponding States" in an oft-cited paper to describe the phenomenon where different systems have very similar behaviors when near a critical point.{{Cite journal |last=Guggenheim |first=E. A. |date=1945-07-01 |title=The Principle of Corresponding States |url=https://pubs.aip.org/jcp/article/13/7/253/186058/The-Principle-of-Corresponding-States |journal=The Journal of Chemical Physics |language=en |volume=13 |issue=7 |pages=253–261 |doi=10.1063/1.1724033 |bibcode=1945JChPh..13..253G |issn=0021-9606|url-access=subscription }}

There are many examples of non-ideal gas models which satisfy this theorem, such as the van der Waals model, the Dieterici model, and so on, that can be found on the page on real gases.

Compressibility factor at the critical point

The compressibility factor at the critical point, which is defined as Z_c=\frac{P_c v_c \mu}{R T_c}, where the subscript c indicates physical quantities measured at the critical point, is predicted to be a constant independent of substance by many equations of state.

The table below for a selection of gases uses the following conventions:

class="wikitable sortable" border="1"
Substance

!P_c [Pa]

!T_c [K]

!v_c [m3/kg]

!Z_c

H2O

|{{val|21.817|e=6}}

|647.3

|{{val|3.154|e=-3}}

| 0.23{{cite book|last=Goodstein|first=David|title=States of Matter|edition=1st|orig-year=1975|year=1985|publisher=General Publishing Company, Ltd.|location=Toronto, Ontario, Canada|isbn=0-486-64927-X|page=[https://archive.org/details/statesofmatter0000good/page/452 452]|chapter=6|trans-chapter=Critical Phenomena and Phase Transitions|url=https://archive.org/details/statesofmatter0000good/page/452}}

4He

|{{val|0.226|e=6}}

|5.2

|{{val|14.43|e=-3}}

| 0.31

He

|{{val|0.226|e=6}}

|5.2

|{{val|14.43|e=-3}}

| 0.30{{cite journal| last = de Boer| first = J.|date=April 1948| title = Quantum theory of condensed permanent gases I the law of corresponding states| journal = Physica| volume = 14| issue = 2–3| pages = 139–148| publisher = Elsevier| location = Utrecht, Netherlands| doi =10.1016/0031-8914(48)90032-9 |bibcode = 1948Phy....14..139D }}

H2

|{{val|1.279|e=6}}

|33.2

|{{val|32.3|e=-3}}

|0.30

Ne

|{{val|2.73|e=6}}

|44.5

|{{val|2.066|e=-3}}

|0.29

N2

|{{val|3.354|e=6}}

|126.2

|{{val|3.2154|e=-3}}

|0.29

Ar

|{{val|4.861|e=6}}

|150.7

|{{val|1.883|e=-3}}

|0.29

Xe

|{{val|5.87|e=6}}

|289.7

|{{val|0.9049|e=-3}}

|0.29

O2

|{{val|5.014|e=6}}

|154.8

|{{val|2.33|e=-3}}

|0.291

CO2

|{{val|7.290|e=6}}

|304.2

|{{val|2.17|e=-3}}

|0.275

SO2

|{{val|7.88|e=6}}

|430.0

|{{val|1.900|e=-3}}

|0.275

CH4

|{{val|4.58|e=6}}

|190.7

|{{val|6.17|e=-3}}

|0.285

C3H8

|{{val|4.21|e=6}}

|370.0

|{{val|4.425|e=-3}}

|0.267

See also

References

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