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Pentane

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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-146.8 ± 0.59kJ/molCcbGood, 1970ALS
Deltafgas-147.1 ± 1.0kJ/molCmPilcher and Chadwick, 1967ALS
Deltafgas-146.4 ± 0.67kJ/molCcbProsen and Rossini, 1945ALS
Quantity Value Units Method Reference Comment
Deltacgas-3535.4 ± 0.96kJ/molCmPilcher and Chadwick, 1967Corresponding «DELTA»fgas = -147.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Deltacgas-3536.6 ± 0.88kJ/molCcbRossini, 1934Corresponding «DELTA»fgas = -145.9 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
gas347.82 ± 0.84J/mol*KN/AMesserly G.H., 1940Scott [ Scott D.W., 1974] has calculated the value of S(298.15 K)=349.49(0.71) J/mol*K on the basis of data [ Messerly G.H., 1940].; GT

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
120.07 ± 0.24298.15Kharin V.E., 1985Experimental data [ Sage B.H., 1937] are less accurate than selected ones. Please also see Hossenlopp I.A., 1981.; GT
127.84 ± 0.26323.15
135.90 ± 0.27348.15
143.95 ± 0.29373.15
151.92 ± 0.30398.15
159.67 ± 0.32423.15
167.37 ± 0.33448.15
168.11450.
174.75 ± 0.35473.15
181.98 ± 0.36498.15
182.39500.
189.08 ± 0.38523.15
195.96550.
209.23600.
221.93650.
232.90700.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
93.55200.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 better agreement with experimental data than the statistical thermodynamics calculation [ Pitzer K.S., 1944, Pitzer K.S., 1946].; GT
112.55273.15
120.0 ± 0.1298.15
120.62300.
152.55400.
182.59500.
208.78600.
231.38700.
250.62800.
266.94900.
281.581000.
293.721100.
304.601200.
313.801300.
322.171400.
330.541500.

Condensed phase thermochemistry data

Go To: Top, Gas 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
DH - E.S. Domalski and E.D. Hearing

Quantity Value Units Method Reference Comment
Deltafliquid-173.5 ± 0.59kJ/molCcbGood, 1970ALS
Deltafliquid-173.1 ± 0.67kJ/molCcbProsen and Rossini, 1945ALS
Quantity Value Units Method Reference Comment
Deltacliquid-3509.0 ± 0.46kJ/molCcbGood, 1970Corresponding «DELTA»fliquid = -173.5 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Deltacliquid-3509.5 ± 0.59kJ/molCcbProsen and Rossini, 1945Corresponding «DELTA»fliquid = -173.0 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Deltacliquid-3509.2 ± 0.75kJ/molCcbProsen and Rossini, 1944Corresponding «DELTA»fliquid = -173.4 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid263.47J/mol*KN/AMesserly, Guthrie, et al., 1967DH
liquid262.67J/mol*KN/AMesserly and Kennedy, 1940DH
liquid259.4J/mol*KN/AParks and Huffman, 1930Extrapolation below 90 K, 56.61 J/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
168.6298.Grigor'ev, Rastorguev, et al., 1975T = 300 to 463 K.; DH
167.19298.15Messerly, Guthrie, et al., 1967T = 12 to 300 K.; DH
167.99290.Messerly and Kennedy, 1940T = 12 to 290 K.; DH
163.2290.0Parks and Huffman, 1930T = 93 to 290 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

Quantity Value Units Method Reference Comment
Tboil309.2 ± 0.2KAVGN/AAverage of 82 out of 95 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus143.4 ± 0.7KAVGN/AAverage of 30 out of 32 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple143.46 ± 0.05KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Tc469.8 ± 0.5KAVGN/AAverage of 27 out of 31 values; Individual data points
Quantity Value Units Method Reference Comment
Pc33.6 ± 0.6barAVGN/AAverage of 20 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.311l/molN/AAmbrose and Tsonopoulos, 1995 
Vc0.3098l/molN/AAftienjew and Zawisza, 1977Uncertainty assigned by TRC = 0.0003 l/mol; TRC
Vc0.295l/molN/ABeattie, Levine, et al., 1951Uncertainty assigned by TRC = 0.006 l/mol; TRC
Vc0.31482l/molN/ASage and Lacey, 1942Uncertainty assigned by TRC = 0.0031 l/mol; TRC
Quantity Value Units Method Reference Comment
rhoc3.22 ± 0.07mol/lAVGN/AAverage of 14 values; Individual data points
Quantity Value Units Method Reference Comment
Deltavap26.5 ± 0.6kJ/molAVGN/AAverage of 11 values; Individual data points

Enthalpy of vaporization

DeltavapH (kJ/mol) Temperature (K) Method Reference Comment
25.79309.2N/AMajer and Svoboda, 1985 
26.200298.15N/AMesserly and Kennedy, 1940P = 68.68 kPa; DH
26.7323.N/APfohl, Riebesell, et al., 2002Based on data from 308. - 423. K.; AC
29.8238.AStephenson and Malanowski, 1987Based on data from 223. - 352. K.; AC
32.3208.AStephenson and Malanowski, 1987Based on data from 143. - 223. K.; AC
26.1365.AStephenson and Malanowski, 1987Based on data from 350. - 422. K.; AC
26.2433.AStephenson and Malanowski, 1987Based on data from 418. - 470. K.; AC
27.9284.EBStephenson and Malanowski, 1987Based on data from 269. - 341. K. See also Osborn and Douslin, 1974.; AC
25.5310.N/ADas, Reed, et al., 1977AC
23.350.N/ADas, Reed, et al., 1977AC
19.7390.N/ADas, Reed, et al., 1977AC
15.1430.N/ADas, Reed, et al., 1977AC
8.5460.N/ADas, Reed, et al., 1977AC

Enthalpy of vaporization

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

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Temperature (K) 260. - 428.
A (kJ/mol) 37.01
alpha -0.1238
beta 0.4121
Tc (K) 469.6
ReferenceMajer and Svoboda, 1985

Entropy of vaporization

DeltavapS (J/mol*K) Temperature (K) Reference Comment
87.88298.15Messerly and Kennedy, 1940P; DH

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
268.8 - 341.373.98921070.617-40.454Osborn and Douslin, 1974Coefficents calculated by NIST from author's data.

Enthalpy of sublimation

DeltasubH (kJ/mol) Temperature (K) Method Reference Comment
42.0143.BBondi, 1963AC

Enthalpy of fusion

DeltafusH (kJ/mol) Temperature (K) Reference Comment
8.401143.47Messerly, Guthrie, et al., 1967DH
8.4149143.46Messerly and Kennedy, 1940DH
8.4143.5Acree, 1991AC
8.376143.4Parks and Huffman, 1930DH

Entropy of fusion

DeltafusS (J/mol*K) Temperature (K) Reference Comment
58.56143.47Messerly, Guthrie, et al., 1967DH
58.66143.46Messerly and Kennedy, 1940DH
58.41143.4Parks and Huffman, 1930DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


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 as indicated in comments:
ALS - H.Y. Afeefy, J.F. Liebman, and S.E. Stein
MS - J.A. Martinho Simões

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

1-Pentene + Hydrogen = Pentane

By formula: C5H10 + H2 = C5H12

Quantity Value Units Method Reference Comment
Deltar-126.6 ± 2.4kJ/molChydMolnar, Rachford, et al., 1984liquid phase; solvent: Dioxane; ALS
Deltar-125.0 ± 1.8kJ/molChydMolnar, Rachford, et al., 1984liquid phase; solvent: Hexane; ALS
Deltar-122.6 ± 2.4kJ/molChydRogers and Skanupong, 1974liquid phase; solvent: Hexane; ALS
Deltar-119. ± 1.kJ/molChydRogers and McLafferty, 1971liquid phase; solvent: Hydrocarbon; ALS

C10H12CrO5 (solution) = Pentane (solution) + C5CrO5 (solution)

By formula: C10H12CrO5 (solution) = C5H12 (solution) + C5CrO5 (solution)

Quantity Value Units Method Reference Comment
Deltar37.3kJ/molN/AMorse, Parker, et al., 1989solvent: Pentane; The reaction enthalpy was derived by using the LPHP value for the enthalpy of cleavage of Cr-CO bond in Cr(CO)6, 154.0 kJ/mol Lewis, Golden, et al., 1984, toghether with a PAC value for the reaction Cr(CO)6(solution) + n-C5H12(solution) = Cr(CO)5(n-C5H12)(solution) + CO(solution), 116.7 kJ/mol Morse, Parker, et al., 1989; MS

Pentane (solution) + Chromium hexacarbonyl (solution) = C10H12CrO5 (solution) + Carbon monoxide (solution)

By formula: C5H12 (solution) + C6CrO6 (solution) = C10H12CrO5 (solution) + CO (solution)

Quantity Value Units Method Reference Comment
Deltar117. ± 11.kJ/molPACMorse, Parker, et al., 1989solvent: Pentane; The reaction enthalpy relies on 0.67 for the quantum yield of CO dissociation; MS

3Hydrogen + 3-Penten-1-yne, (Z)- = Pentane

By formula: 3H2 + C5H6 = C5H12

Quantity Value Units Method Reference Comment
Deltar-405. ± 0.4kJ/molChydRoth, Adamczak, et al., 1991liquid phase; ALS
Deltar-400. ± 4.6kJ/molChydSkinner and Snelson, 1959liquid phase; solvent: Acetic acid; ALS

3Hydrogen + 3-Penten-1-yne, (E)- = Pentane

By formula: 3H2 + C5H6 = C5H12

Quantity Value Units Method Reference Comment
Deltar-406. ± 1.kJ/molChydRoth, Adamczak, et al., 1991liquid phase; ALS
Deltar-402. ± 2.kJ/molChydSkinner and Snelson, 1959liquid phase; solvent: Acetic acid; ALS

2Hydrogen + 1,4-Pentadiene = Pentane

By formula: 2H2 + C5H8 = C5H12

Quantity Value Units Method Reference Comment
Deltar-252.0 ± 0.63kJ/molChydKistiakowsky, Ruhoff, et al., 1936gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -254.3 ± 0.63 kJ/mol; At 355 °K; ALS

Phenol (solution) + C5H11BrMg (solution) = C6H5BrMgO (solution) + Pentane (solution)

By formula: C6H6O (solution) + C5H11BrMg (solution) = C6H5BrMgO (solution) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-202.5 ± 4.2kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

C5H11BrMg (solution) + Hydrogen bromide (g) = Pentane (solution) + Br2Mg (solution)

By formula: C5H11BrMg (solution) + HBr (g) = C5H12 (solution) + Br2Mg (solution)

Quantity Value Units Method Reference Comment
Deltar-306.3 ± 2.2kJ/molRSCHolm, 1981solvent: Diethyl ether; MS

Ethanol (solution) + C5H11BrMg (solution) = C2H5BrMgO (solution) + Pentane (solution)

By formula: C2H6O (solution) + C5H11BrMg (solution) = C2H5BrMgO (solution) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-199.6 ± 4.2kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

C5H11BrMg (solution) + Methylamine (solution) = CH4BrMgN (solution) + Pentane (solution)

By formula: C5H11BrMg (solution) + CH5N (solution) = CH4BrMgN (solution) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-130.5 ± 2.5kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

2Hydrogen + Cyclopropane,ethenyl- = Pentane

By formula: 2H2 + C5H8 = C5H12

Quantity Value Units Method Reference Comment
Deltar-274. ± 0.8kJ/molChydRoth, Kirmse, et al., 1982liquid phase; solvent: Isooctane; ALS

C5O5W (g) + Pentane (g) = C10H12O5W (g)

By formula: C5O5W (g) + C5H12 (g) = C10H12O5W (g)

Quantity Value Units Method Reference Comment
Deltar-44. ± 13.kJ/molEqGBrown, Ishikawa, et al., 1990Temperature range: ca. 300-350 K; MS

C5H11BrMg (solution) + Methane (solution) = Pentane (solution) + CH3BrMg (solution)

By formula: C5H11BrMg (solution) + CH4 (solution) = C5H12 (solution) + CH3BrMg (solution)

Quantity Value Units Method Reference Comment
Deltar-15.1 ± 4.2kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

Propanedinitrile (solution) + C5H11BrMg (solution) = C3HBrMgN2 (solution) + Pentane (solution)

By formula: C3H2N2 (solution) + C5H11BrMg (solution) = C3HBrMgN2 (solution) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-203.3kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

Diphenylamine (solution) + C5H11BrMg (solution) = C12H10BrMgN (solution) + Pentane (solution)

By formula: C12H11N (solution) + C5H11BrMg (solution) = C12H10BrMgN (solution) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-118.8kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

C5H11BrMg (solution) + Trifluoroacetic acid (solution) = C2BrF3MgO2 (solution) + Pentane (solution)

By formula: C5H11BrMg (solution) + C2HF3O2 (solution) = C2BrF3MgO2 (solution) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-273.6kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

C5H11BrMg (solution) + Phenol, pentafluoro- (solution) = C6BrF5MgO (cr) + Pentane (solution)

By formula: C5H11BrMg (solution) + C6HF5O (solution) = C6BrF5MgO (cr) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-233.9kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

C5H11BrMg (solution) + Ethanol, 2,2,2-trifluoro- (solution) = C2H2BrF3MgO (solution) + Pentane (solution)

By formula: C5H11BrMg (solution) + C2H3F3O (solution) = C2H2BrF3MgO (solution) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-199.6kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

Methyl Alcohol (solution) + C5H11BrMg (solution) = CH3BrMgO (cr) + Pentane (solution)

By formula: CH4O (solution) + C5H11BrMg (solution) = CH3BrMgO (cr) + C5H12 (solution)

Quantity Value Units Method Reference Comment
Deltar-219.7kJ/molRSCHolm, 1983solvent: Diethyl ether; MS

2Hydrogen + 1,3-Pentadiene = Pentane

By formula: 2H2 + C5H8 = C5H12

Quantity Value Units Method Reference Comment
Deltar-226.4 ± 0.63kJ/molChydDolliver, Gresham, et al., 1937gas phase; At 355 °K; ALS

Pentane = Butane, 2-methyl-

By formula: C5H12 = C5H12

Quantity Value Units Method Reference Comment
Deltar-7.786kJ/molEqkPines, Kvetinskas, et al., 1945gas phase; Heat of isomerization; ALS

Hydrogen + 2-Pentene, (Z)- = Pentane

By formula: H2 + C5H10 = C5H12

Quantity Value Units Method Reference Comment
Deltar-117.7 ± 0.8kJ/molChydEgger and Benson, 1966gas phase; ALS

Hydrogen + 2-Pentene, (E)- = Pentane

By formula: H2 + C5H10 = C5H12

Quantity Value Units Method Reference Comment
Deltar-113.8 ± 0.8kJ/molChydEgger and Benson, 1966gas phase; ALS

IR Spectrum

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

Data compiled by: Coblentz Society, Inc.

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


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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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, 1998.
NIST MS number 291244

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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.

Good, 1970
Good, W.D., The enthalpies of combustion and formation of the isomeric pentanes, J. Chem. Thermodyn., 1970, 2, 237-244. [all data]

Pilcher and Chadwick, 1967
Pilcher, G.; Chadwick, J.D.M., Measurements of heats of combustion by flame calorimetry. Part 4.-n-Pentane, isopentane, neopentane, Trans. Faraday Soc., 1967, 63, 2357-2361. [all data]

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]

Rossini, 1934
Rossini, F.D., Calorimetric determination of the heats of combustion of ethane, propane, normal butane, and normal pentane, J. Res. NBS, 1934, 12, 735-750. [all data]

Messerly G.H., 1940
Messerly G.H., The heat capacity and entropy, heats of fusion and vaporization and the vapor pressure of n-pentane, J. Am. Chem. Soc., 1940, 62, 2988-2991. [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]

Kharin V.E., 1985
Kharin V.E., Isobaric heat capacity of n-pentane in the vapor phase, Izv. Vyssh. Ucheb. Zaved., Neft. Gaz, 1985, 28, 63-66. [all data]

Sage B.H., 1937
Sage B.H., Phase equilibria in hydrocarbon systems. XX. Isobaric heat capacity of gaseous propane, n-butane, isobutane, and n-pentane, Ind. Eng. Chem., 1937, 29, 1309-1314. [all data]

Hossenlopp I.A., 1981
Hossenlopp I.A., Vapor heat capacities and enthalpies of vaporization of five alkane hydrocarbons, J. Chem. Thermodyn., 1981, 13, 415-421. [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]

Pitzer K.S., 1944
Pitzer K.S., Thermodynamics of gaseous paraffins. Specific heat and related properties, Ind. Eng. Chem., 1944, 36, 829-831. [all data]

Pitzer K.S., 1946
Pitzer K.S., The entropies and related properties of branched paraffin hydrocarbons, Chem. Rev., 1946, 39, 435-447. [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]

Messerly, Guthrie, et al., 1967
Messerly, J.F.; Guthrie, G.B.; Todd, S.S.; Finke, H.L., Low-temperature thermal data for n-pentane, n-heptadecane, and n-octadecane, J. Chem. Eng. Data, 1967, 12, 338-346. [all data]

Messerly and Kennedy, 1940
Messerly, G.H.; Kennedy, R.M., The heat capacity and entropy, heats of fusion and vaporization and the vapor pressure of n-pentane, J. Am. Chem. Soc., 1940, 62, 2988-2991. [all data]

Parks and Huffman, 1930
Parks, G.S.; Huffman, H.M., Thermal data on organic compounds. IX. A study of the effect of unsaturation on the heat capacities, entropies and free energies of some hydrocarbons and other compounds, J. Am. Chem. Soc., 1930, 52, 4381-4391. [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]

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]

Aftienjew and Zawisza, 1977
Aftienjew, J.; Zawisza, A., High-pressure liquid vapour-equilibria, critical state and p(V,T,x) up to 503.15 and 4.560 MPa for n-pentane + n-perfluoropentane, J. Chem. Thermodyn., 1977, 9, 153-165. [all data]

Beattie, Levine, et al., 1951
Beattie, J.A.; Levine, S.W.; Douslin, D.R., The vapor pressure and critical constants of normal pentane, J. Am. Chem. Soc., 1951, 73, 4431. [all data]

Sage and Lacey, 1942
Sage, B.H.; Lacey, W.N., Phase equilibria in hydrocarbon systems. Thermodynamic properties of n- pentane., Ind. Eng. Chem., 1942, 34, 730-737. [all data]

Majer and Svoboda, 1985
Majer, V.; Svoboda, V., Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]

Pfohl, Riebesell, et al., 2002
Pfohl, Oliver; Riebesell, Christine; Dohrn, Ralf, Measurement and calculation of phase equilibria in the system n-pentane + poly(dimethylsiloxane) at 308.15--423.15 K, Fluid Phase Equilibria, 2002, 202, 2, 289-306, https://doi.org/10.1016/S0378-3812(02)00123-1 . [all data]

Stephenson and Malanowski, 1987
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Notes

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