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Decane

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, Mass spectrum (electron ionization), References, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
ALS - H.Y. Afeefy, J.F. Liebman, and S.E. Stein
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Deltafgas-249.7 ± 1.1kJ/molCcbProsen and Rossini, 1945ALS
Quantity Value Units Method Reference Comment
gas545.8 ± 1.1J/mol*KN/AScott D.W., 1974This reference does not contain the original experimental data. Experimental entropy value is based on the results [ Messerly J.F., 1967] for S(liquid).; GT

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
179.08200.Scott D.W., 1974, 2Recommended values were obtained from the consistent correlation scheme for alkanes [ Scott D.W., 1974, Scott D.W., 1974, 2]. This approach gives a good agreement with experimental data available for alkanes. However, large uncertainties could be expected at high temperatures.; GT
217.90273.15
233.1 ± 0.6298.15
234.18300.
297.98400.
356.43500.
405.85600.
446.43700.
479.90800.
508.36900.
531.791000.
551.871100.
569.441200.
585.761300.
598.311400.
610.861500.

Condensed phase thermochemistry data

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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
ALS - H.Y. Afeefy, J.F. Liebman, and S.E. Stein
DH - E.S. Domalski and E.D. Hearing

Quantity Value Units Method Reference Comment
Deltafliquid-301.0 ± 1.1kJ/molCcbProsen and Rossini, 1945ALS
Quantity Value Units Method Reference Comment
Deltacliquid-6778.33 ± 0.88kJ/molCcbProsen and Rossini, 1945Corresponding «DELTA»fliquid = -300.9 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Deltacliquid-6778.6 ± 1.5kJ/molCcbProsen and Rossini, 1944Corresponding «DELTA»fliquid = -300.6 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Deltacliquid-6774.2kJ/molCcbJessup, 1937Corresponding «DELTA»fliquid = -305.0 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid425.89J/mol*KN/AFinke, Gross, et al., 1954DH
liquid428.9J/mol*KN/AHuffman, Parks, et al., 1931Extrapolation below 90 K, 92.05 J/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
314.45298.9Czarnota, 1993p = 0.1 MPa.; DH
323.87318.15Banipal, Garg, et al., 1991T = 313 to 373 K. p = 0.1 MPa.; DH
315.46298.15Trejo, Costas, et al., 1991DH
315.46298.15Andreoli-Ball, Patterson, et al., 1988DH
315.32298.15Costas, Huu, et al., 1988DH
315.0298.23Kuznetsov, Kharin, et al., 1988T = 293 to 420 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.214 kJ/kg*K.; DH
313.46298.15Perez-Casas, Aicart, et al., 1988DH
313.13298.15Pintos, Bravo, et al., 1988DH
315.46298.15Wilhelm, Inglese, et al., 1987DH
313.56298.15Gates, Wood, et al., 1986T = 298.15 to 368.15 K.; DH
315.46298.15Tardajos, Aicart, et al., 1986DH
313.24298.15Baluja, Bravo, et al., 1985DH
314.82298.15Costas and Patterson, 1985T = 283.15, 298.15, 313.15 K.; DH
312.99298.15Lainez, Rodrigo, et al., 1985DH
313.09298.15Lainez, Roux-Desgranges, et al., 1985DH
313.09298.15Lainez, Wilhelm, et al., 1985DH
313.93298.15Grolier, Inglese, et al., 1984DH
314.21298.15Roux, Grolier, et al., 1984DH
310.26293.15Siddiqi, Svejda, et al., 1983DH
312.5298.15Wilhelm, Inglese, et al., 1982DH
312.8298.Zaripov, 1982T = 298, 323, 363 K.; DH
313.3298.15Grolier, Hamedi, et al., 1979DH
311.7298.Grigor'ev, Rastorguev, et al., 1975T = 300 to 463 K.; DH
314.47298.15Finke, Gross, et al., 1954T = 12 to 300 K.; DH
312.29299.8Schlinger and Sage, 1952T = 80 to 200°F.; DH
313.97298.15Osborne and Ginnings, 1947T = 278 to 318 K.; DH
311.3297.7Huffman, Parks, et al., 1931T = 91 to 298 K. Value is unsmoothed experimental datum.; DH
309.6295.5Parks, Huffman, et al., 1930T = 242 to 296 K. Value is unsmoothed experimental datum.; DH

Phase change data

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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
BS - R.L. Brown and S.E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, M. Frenkel director
AC - W.E. Acree, Jr., J.S. Chickos
ALS - H.Y. Afeefy, J.F. Liebman, and S.E. Stein
DH - E.S. Domalski and E.D. Hearing
CAL - J.S. Chickos, W.E. Acree, Jr., J.F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis

Quantity Value Units Method Reference Comment
Tboil447.2 ± 0.3KAVGN/AAverage of 34 out of 43 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus243.3 ± 0.6KAVGN/AAverage of 23 out of 25 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple243.4 ± 0.3KAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
Tc617.8 ± 0.7KAVGN/AAverage of 16 out of 18 values; Individual data points
Quantity Value Units Method Reference Comment
Pc21.1 ± 0.8barAVGN/AAverage of 11 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.624l/molN/AAmbrose and Tsonopoulos, 1995 
Quantity Value Units Method Reference Comment
rhoc1.60 ± 0.05mol/lN/AAmbrose and Tsonopoulos, 1995 
rhoc1.67mol/lN/ASteele, 1992Uncertainty assigned by TRC = 0.070 mol/l; TRC
rhoc1.60mol/lN/AAnselme, Gude, et al., 1990Uncertainty assigned by TRC = 0.04 mol/l; TRC
rhoc1.67mol/lN/AKnipmeyer, Archer, et al., 1989Uncertainty assigned by TRC = 0.070 mol/l; TRC
rhoc1.595mol/lN/AGehrig and Lentz, 1983Uncertainty assigned by TRC = 0.04 mol/l; TRC
Quantity Value Units Method Reference Comment
Deltavap51.3 ± 0.3kJ/molAVGN/AAverage of 12 values; Individual data points
Quantity Value Units Method Reference Comment
Deltasub80.3kJ/molBSwain, Kwan, et al., 1980AC
Deltasub82.4kJ/molHBondi, 1963See also Chickos, Hosseini, et al., 1993.; AC

Enthalpy of vaporization

DeltavapH (kJ/mol) Temperature (K) Method Reference Comment
38.75447.3N/AMajer and Svoboda, 1985 
48.3339.GCMokbel, Razzouk, et al., 2007Based on data from 324. - 402. K.; AC
46.6352.N/ABatiu, 2002Based on data from 337. - 376. K.; AC
51.5299.CViton, Chavret, et al., 1996AC
50.5314.CViton, Chavret, et al., 1996AC
50.1324.CViton, Chavret, et al., 1996AC
49.2334.CViton, Chavret, et al., 1996AC
42.5424.N/ALee, Dempsey, et al., 1992Based on data from 409. - 584. K.; AC
48.1340.EB,IPChirico, Nguyen, et al., 1989Based on data from 268. - 490. K.; AC
53.8267.AStephenson and Malanowski, 1987Based on data from 252. - 383. K.; AC
41.7462.AStephenson and Malanowski, 1987Based on data from 447. - 526. K.; AC
38.6539.AStephenson and Malanowski, 1987Based on data from 524. - 617. K.; AC
45.3388.N/AStephenson and Malanowski, 1987Based on data from 373. - 443. K. See also Varushchenko, Belikova, et al., 1970.; AC
50.3313.GSAllemand, Jose, et al., 1986Based on data from 298. - 347. K.; AC
49.8 ± 1.7308. - 351.N/ABeckhaus, Ruchardt, et al., 1984AC
55.9258.N/ACarruth and Kobayashi, 1973Based on data from 243. - 310. K.; AC
45.5383.MMWillingham, Taylor, et al., 1945Based on data from 368. - 440. K.; AC

Enthalpy of vaporization

ΔvapH = A exp(-βTr) (1 − Tr)β
    ΔvapH = Enthalpy of vaporization (at saturation pressure) (kJ/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) A (kJ/mol) beta Tc (K) Reference Comment
298. - 444.74.380.3238617.4Majer and Svoboda, 1985 

Antoine Equation Parameters

log10(P) = A − (B / (T + C))
    P = vapor pressure (bar)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
243.49 - 310.590.21021440.616-156.896Carruth and Kobayashi, 1973Coefficents calculated by NIST from author's data.
367.63 - 448.274.078571501.268-78.67Williamham, Taylor, et al., 1945 

Enthalpy of sublimation

DeltasubH (kJ/mol) Temperature (K) Method Reference Comment
84.8243.BBondi, 1963AC

Enthalpy of fusion

DeltafusH (kJ/mol) Temperature (K) Method Reference Comment
28.715243.51N/AFinke, Gross, et al., 1954DH
27.6243.DSCMarti, Kaisersberger, et al., 2004AC
28.7243.5N/ADomalski and Hearing, 1996AC
28.778243.1N/AHuffman, Parks, et al., 1931DH

Entropy of fusion

DeltafusS (J/mol*K) Temperature (K) Reference Comment
117.92243.51Finke, Gross, et al., 1954DH
117.99243.5Domalski and Hearing, 1996CAL
118.4243.1Huffman, Parks, et al., 1931DH

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Reaction thermochemistry data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, IR Spectrum, Mass spectrum (electron ionization), References, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled by: H.Y. Afeefy, J.F. Liebman, and S.E. Stein

Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.

Individual Reactions

Hydrogen + 1-Decene = Decane

By formula: H2 + C10H20 = C10H22

Quantity Value Units Method Reference Comment
Deltar-124.2 ± 1.2kJ/molChydRogers and Skanupong, 1974liquid phase; solvent: Hexane
Deltar-125.1 ± 1.3kJ/molChydBretschneider and Rogers, 1970liquid phase; solvent: galcial acetic acid

3Hydrogen + 3-Decen-1-yne, (Z)- = Decane

By formula: 3H2 + C10H16 = C10H22

Quantity Value Units Method Reference Comment
Deltar-400. ± 2.kJ/molChydSkinner and Snelson, 1959liquid phase; solvent: Acetic acid

3Hydrogen + 3-Decen-1-yne, (E)- = Decane

By formula: 3H2 + C10H16 = C10H22

Quantity Value Units Method Reference Comment
Deltar-401.3 ± 0.8kJ/molChydSkinner and Snelson, 1959liquid phase; solvent: Acetic acid

Hydrogen + (Z)-5-Decene = Decane

By formula: H2 + C10H20 = C10H22

Quantity Value Units Method Reference Comment
Deltar-119.5 ± 1.5kJ/molChydRogers and Siddiqui, 1975liquid phase; solvent: n-Hexane

2Hydrogen + 2-Decyne = Decane

By formula: 2H2 + C10H18 = C10H22

Quantity Value Units Method Reference Comment
Deltar-273.1 ± 2.1kJ/molChydRogers, Dagdagan, et al., 1979liquid phase; solvent: Hexane

2Hydrogen + 3-Decyne = Decane

By formula: 2H2 + C10H18 = C10H22

Quantity Value Units Method Reference Comment
Deltar-271.4 ± 2.0kJ/molChydRogers, Dagdagan, et al., 1979liquid phase; solvent: Hexane

2Hydrogen + 4-Decyne = Decane

By formula: 2H2 + C10H18 = C10H22

Quantity Value Units Method Reference Comment
Deltar-269.4 ± 1.7kJ/molChydRogers, Dagdagan, et al., 1979liquid phase; solvent: Hexane

2Hydrogen + 5-Decyne = Decane

By formula: 2H2 + C10H18 = C10H22

Quantity Value Units Method Reference Comment
Deltar-268.2 ± 2.0kJ/molChydRogers, Dagdagan, et al., 1979liquid phase; solvent: Hexane

2Hydrogen + 1-Decyne = Decane

By formula: 2H2 + C10H18 = C10H22

Quantity Value Units Method Reference Comment
Deltar-291.4 ± 2.1kJ/molChydRogers, Dagdagan, et al., 1979liquid phase; solvent: Hexane

IR Spectrum

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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled by: NIST Mass Spec Data Center, S.E. Stein, director

Gas Phase Spectrum

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IR spectrum
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Additional Data

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Owner NIST Standard Reference Data Program
Collection (C) 2018 copyright by the U.S. Secretary of Commerce
on behalf of the United States of America. All rights reserved.
Origin Sadtler Research Labs Under US-EPA Contract
State gas

This IR spectrum is from the NIST/EPA Gas-Phase Infrared Database .


Mass spectrum (electron ionization)

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, References, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled by: NIST Mass Spec Data Center, S.E. Stein, director

Spectrum

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Mass spectrum
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Additional Data

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Owner NIST Mass Spectrometry Data Center
Collection (C) 2014 copyright by the U.S. Secretary of Commerce
on behalf of the United States of America. All rights reserved.
Origin NIST Mass Spectrometry Data Center, 1990.
NIST MS number 114147

All mass spectra in this site (plus many more) are available from the NIST/EPA/NIH Mass Spectral Library. Please see the following for information about the library and its accompanying search program.


References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, Mass spectrum (electron ionization), Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Prosen and Rossini, 1945
Prosen, E.J.; Rossini, F.D., Heats of combustion and formation of the paraffin hydrocarbons at 25° C, J. Res. NBS, 1945, 263-267. [all data]

Scott D.W., 1974
Scott D.W., Correlation of the chemical thermodynamic properties of alkane hydrocarbons, J. Chem. Phys., 1974, 60, 3144-3165. [all data]

Messerly J.F., 1967
Messerly J.F., Low-temperature thermal data for n-pentane, n-heptadecane, and n-octadecane. Revised thermodynamic functions for the n-alkanes, C5-C18, J. Chem. Eng. Data, 1967, 12, 338-346. [all data]

Scott D.W., 1974, 2
Scott D.W., Chemical Thermodynamic Properties of Hydrocarbons and Related Substances. Properties of the Alkane Hydrocarbons, C1 through C10 in the Ideal Gas State from 0 to 1500 K. U.S. Bureau of Mines, Bulletin 666, 1974. [all data]

Prosen and Rossini, 1944
Prosen, E.J.; Rossini, F.D., Heats of combustion of eight normal paraffin hydrocarbons in the liquid state, J. Res. NBS, 1944, 33, 255-272. [all data]

Jessup, 1937
Jessup, R.S., Heats of combustion of the liquid normal paraffin hydrocarbons from hexane to dodecane, J. Res. NBS, 1937, 18, 114-128. [all data]

Finke, Gross, et al., 1954
Finke, H.L.; Gross, M.E.; Waddington, G.; Huffman, H.M., Low-temperature thermal data for the nine normal paraffin hydrocarbons from octane to hexadecane, J. Am. Chem. Soc., 1954, 76, 333-341. [all data]

Huffman, Parks, et al., 1931
Huffman, H.M.; Parks, G.S.; Barmore, M., Thermal data on organic compounds. X. Further studies on the heat capacities, entropies and free energies of hydrocarbons, J. Am. Chem. Soc., 1931, 53, 3876-3888. [all data]

Czarnota, 1993
Czarnota, I., Heat capacity of decane at high pressures, J. Chem. Thermodynam., 1993, 25, 639-642. [all data]

Banipal, Garg, et al., 1991
Banipal, T.S.; Garg, S.K.; Ahluwalia, J.C., Heat capacities and densities of liquid n-octane, n-nonane, n-decane, and n-hexadecane at temperatures from 318.15 to 373.15 K and at pressures up to 10 MPa, J. Chem. Thermodynam., 1991, 23, 923-931. [all data]

Trejo, Costas, et al., 1991
Trejo, L.M.; Costas, M.; Patterson, D., Excess heat capacity of organic mixtures, Internat. DATA Series, Selected Data Mixt., 1991, Ser. [all data]

Andreoli-Ball, Patterson, et al., 1988
Andreoli-Ball, L.; Patterson, D.; Costas, M.; Caceres-Alonso, M., Heat capacity and corresponding states in alkan-1-ol-n-alkane systems, J. Chem. Soc., Faraday Trans. 1, 1988, 84(11), 3991-4012. [all data]

Costas, Huu, et al., 1988
Costas, M.; Huu, V.T.; Patterson, D.; Caceres-Alonso, M.; Tardajos, G.; Aicart, E., Liquid structure and second-order mixing functions for l-chloronaphthalene with linear and branched alkanes, J. Chem. Soc., Faraday Trans., 1988, 1 84(5), 1603-1616. [all data]

Kuznetsov, Kharin, et al., 1988
Kuznetsov, M.A.; Kharin, V.E.; Gerasimov, A.A.; Grigor'ev, M.D., Isobaric heat capacity of n-alkanes C7 to C10 at temperatures 293 to 630 K and pressures up to 60 MPa, Izv. Vyssh. Ucheb. Zabed., Neft i Gaz, 1988, 31(11), 49-52. [all data]

Perez-Casas, Aicart, et al., 1988
Perez-Casas, S.; Aicart, E.; Trojo, L.M.; Costas, M., Excess heat capacity. Chlorobenzene-2,2,4,4,6,8,8-heptamethylnonane, Int. Data Ser., Sel. Data Mixtures, 1988, (2)A, 123. [all data]

Pintos, Bravo, et al., 1988
Pintos, M.; Bravo, R.; Baluja, M.C.; Paz Andrade, M.I.; Roux-Desgranges, G.; Grolier, J.-P.E., Can. J. Chem., 1988, 1179. [all data]

Wilhelm, Inglese, et al., 1987
Wilhelm, E.; Inglese, A.; Roux, A.H.; Grolier, J.-P.E., Excess enthalpy, excess heat capacity and excess volume of 1,2,4-trimethylbenzene +, and 1-methylnaphthalene + an n-alkane, Fluid Phase Equilibria, 1987, 34, 49-67. [all data]

Gates, Wood, et al., 1986
Gates, J.A.; Wood, R.H.; Cobos, J.C.; Casanova, C.; Roux, A.H.; Roux-Desgranges, G.; Grolier, J.-P.E., Densities and heat capacities of 1-butanol + n-decane from 298 K to 400 K, Fluid Phase Equilib., 1986, 27, 137-151. [all data]

Tardajos, Aicart, et al., 1986
Tardajos, G.; Aicart, E.; Costas, M.; Patterson, D., Liquid structure and second-order mixing functions for benzene, toluene, and p-xylene with n-alkanes, J. Chem. Soc., Faraday Trans., 1986, 1 82, 2977-2987. [all data]

Baluja, Bravo, et al., 1985
Baluja, M.C.; Bravo, R.; Pintos, M.; Paz Andrade, M.I.; Roux-Desgranges, G.; Grolier, J.-P.E., Unusual dependence on concentration of the excess heat capacities of ester solutions in alkanes, Calorim. Anal. Therm., 1985, 16, 138-144. [all data]

Costas and Patterson, 1985
Costas, M.; Patterson, D., Self-association of alcohols in inert solvents, J. Chem. Soc., Faraday Trans. 1, 1985, 81, 635-654. [all data]

Lainez, Rodrigo, et al., 1985
Lainez, A.; Rodrigo, M.; Roux, A.H.; Grolier, J.-P.E.; Wilhelm, E., Relations between structure and thermodynamic properties. Heat capacities of polar substances (nitrobenzene and benzonitrile) in alkane solutions, Calorim. Anal. Therm., 1985, 16, 153-158. [all data]

Lainez, Roux-Desgranges, et al., 1985
Lainez, A.; Roux-Desgranges, G.; Grolier, J.-P.E.; Wilhelm, E., Mixtures of alkanes with polar molecules showing integral rotation: an unusual composition dependence of CpE of 1,2-dichloroethane + an n-alkane, Fluid Phase Equilib., 1985, 20, 47-56. [all data]

Lainez, Wilhelm, et al., 1985
Lainez, A.; Wilhelm, E.; Roux-Desgranges, G.; Grolier, J.-P.E., Excess molar quantities of (a halogenated n-alkane + an n-alkane). A comparative study of mixtures containing either 1-chlorobutane or 1,4-dichlorobutane, J. Chem. Thermodynam., 1985, 17, 1153-1161. [all data]

Grolier, Inglese, et al., 1984
Grolier, J.-P.E.; Inglese, A.; Wilhelm, E., Excess molar heat capacities of (1,4-dioxane + an n-alkane): an unusual composition dependence, J. Chem. Thermodynam., 1984, 16, 67-71. [all data]

Roux, Grolier, et al., 1984
Roux, A.H.; Grolier, J.-P.E.; Inglese, A.; Wilhelm, E., Excess molar enthalpies, excess molar heat capacities and excess molar volumes of (fluorobenzene + an n-alkane), Ber. Bunsenges. Phys. Chem., 1984, 88, 986-992. [all data]

Siddiqi, Svejda, et al., 1983
Siddiqi, M.A.; Svejda, P.; Kohler, F., A generalized van der Waals equation of state II. Excess heat capacities of mixtures containing cycloalkanes (C5,C6), methylcycloalkanes (C5,C6) and n-decane, Ber. Bunsenges. Phys. Chem., 1983, 87, 1176-1181. [all data]

Wilhelm, Inglese, et al., 1982
Wilhelm, E.; Inglese, A.; Quint, J.R.; Grolier, J.-P.E., Molar excess volumes and excess heat capacities of (1,2,4-trichlorobenzene + an alkane), J. Chem. Thermodynam., 1982, 14, 303-308. [all data]

Zaripov, 1982
Zaripov, Z.I., Experimental study of the isobaric heat capacity of liquid organic compounds with molecular weights of up to 4000 a.e.m., 1982, Teplomassoobmen Teplofiz. [all data]

Grolier, Hamedi, et al., 1979
Grolier, J-P.E.; Hamedi, M.H.; Wilhelm, E.; Kehiaian, H.V., Excess heat capacities of binary mixtures of carbon tetrachloride with n-alkanes at 298.15 K, Thermochim. Acta, 1979, 31, 79-84. [all data]

Grigor'ev, Rastorguev, et al., 1975
Grigor'ev, B.A.; Rastorguev, Yu.L.; Yanin, G.S., Experimental determination of the isobaric specific heat of n-alkanes, Iz. Vyssh. Uchebn. Zaved. Neft Gaz 18, 1975, No.10, 63-66. [all data]

Schlinger and Sage, 1952
Schlinger, W.G.; Sage, B.H., Isobaric heat capacities at bubble point. cis-2-butene, isopropylbenzene, and n-decane, Ind. Eng. Chem., 1952, 44, 2454-2456. [all data]

Osborne and Ginnings, 1947
Osborne, N.S.; Ginnings, D.C., Measurements of heat of vaporization and heat capacity of a number of hydrocarbons, J. Res. NBS, 1947, 39, 453-477. [all data]

Parks, Huffman, et al., 1930
Parks, G.S.; Huffman, H.M.; Thomas, S.B., Thermal data on organic compounds. VI. The heat capacities, entropies and free energies of some saturated, non-benzenoid hydrocarbons, J. Am. Chem. Soc., 1930, 52, 1032-1041. [all data]

Ambrose and Tsonopoulos, 1995
Ambrose, D.; Tsonopoulos, C., Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkenes, J. Chem. Eng. Data, 1995, 40, 531-546. [all data]

Steele, 1992
Steele, W.V., Personal Commun. 1992 1992, 1992. [all data]

Anselme, Gude, et al., 1990
Anselme, M.J.; Gude, M.; Teja, A.S., The Critical Temperatures and Densities of the n-Alkanes from Pentane to Octadecane, Fluid Phase Equilib., 1990, 57, 317-26. [all data]

Knipmeyer, Archer, et al., 1989
Knipmeyer, S.E.; Archer, D.G.; Chirico, R.D.; Gammon, B.E.; Hossenlopp, I.A.; Nguyen, A.; Smith, N.K.; Steele, W.V.; Strube, M.M., High-temperature enthalpy and critical property measurements using differential scanning calorimeter, Fluid Phase Equilib., 1989, 52, 185. [all data]

Gehrig and Lentz, 1983
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Notes

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