Propene

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, 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 - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas4.879kcal/molEqkFuruyama, Golden, et al., 1969ALS
Δfgas4.879kcal/molCmLacher, Walden, et al., 1950Heat of hydrobromination; ALS
Quantity Value Units Method Reference Comment
Δcgas-491.83 ± 0.27kcal/molCmWiberg and Fenoglio, 1968Corresponding Δfgas = 4.73 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcgas-491.8 ± 0.1kcal/molCmRossini and Knowlton, 1937Reanalyzed by Cox and Pilcher, 1970, Original value = -491.74 ± 0.15 kcal/mol; Corresponding Δfgas = 4.71 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
8.21050.Thermodynamics Research Center, 1997p=1 bar. Recommended entropies and heat capacities are in good agreement with other statistically calculated values [ Crawford B.L., 1939, Kilpatrick J.E., 1946, Kilpatrick J.E., 1947, Chao J., 1975] as well as with ab initio value of S(298.15 K)=266.82 J/mol*K [ East A.L.L., 1997].; GT
9.338100.
10.60150.
12.01200.
14.45273.15
15.37298.15
15.44300.
19.23400.
22.75500.
25.813600.
28.463700.
30.765800.
32.772900.
34.5221000.
36.0491100.
37.3801200.
38.5401300.
39.5511400.
40.4351500.
42.1941750.
43.4752000.
44.4292250.
45.1512500.
45.7072750.
46.1473000.

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
10.64148.2Bier K., 1974Please also see Kistiakowsky G.B., 1940, Kistiakowsky G.B., 1940, 2, Telfair D., 1942.; GT
10.86157.6
12.48213.1
12.69220.1
12.83223.7
13.97258.0
14.29270.
14.36 ± 0.031272.29
14.69280.
15.16291.1
15.25 ± 0.031298.15
15.47 ± 0.031299.33
15.47300.
16.23320.
16.22 ± 0.033323.15
16.74 ± 0.041333.86
16.98340.
17.16 ± 0.033348.15
17.72360.
17.80 ± 0.036365.15
17.93 ± 0.02367.11
18.11 ± 0.036373.15
19.08 ± 0.038378.15
18.44380.
19.16400.
19.88420.
19.98 ± 0.041423.15
20.58440.
20.90 ± 0.041448.15
21.28460.
21.79 ± 0.043473.15
21.97480.
22.65500.
22.99510.

Condensed phase thermochemistry data

Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, 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: Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
liquid46.77cal/mol*KN/AChao, Hall, et al., 1983 

Constant pressure heat capacity of liquid

Cp,liquid (cal/mol*K) Temperature (K) Reference Comment
24.4298.15Chao, Hall, et al., 1983T = 14 to 340 K.
23.6300.Auerbach, Sage, et al., 1950T = 300 to 344 K. Datum at 80°C is Cp at the bubble point, 0.5615 Btu/lb*R.
22.01230.Powell and Giauque, 1939T = 14 to 225 K.
21.5210.3Huffman, Parks, et al., 1931T = 69 to 210 K. Value is unsmoothed experimental datum.

Phase change data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Henry's Law data, Gas phase ion energetics data, 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:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
DH - Eugene S. Domalski and Elizabeth D. Hearing
AC - William E. Acree, Jr., James S. Chickos

Quantity Value Units Method Reference Comment
Tboil225.6 ± 0.6KAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus88.0KN/AStreng, 1971Uncertainty assigned by TRC = 0.3 K; TRC
Tfus87.9KN/AHaselden and Snowden, 1962Uncertainty assigned by TRC = 0.4 K; TRC
Tfus88.25KN/AParks and Huffman, 1931Uncertainty assigned by TRC = 1. K; TRC
Tfus87.95KN/ACoffin and Maass, 1927Uncertainty assigned by TRC = 0.6 K; TRC
Quantity Value Units Method Reference Comment
Ttriple87.8 ± 0.8KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Ptriple9.38atmN/AAngus, Armstrong, et al., 1980Uncertainty assigned by TRC = 0.15 atm; TRC
Quantity Value Units Method Reference Comment
Tc365.2 ± 0.8KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Pc45.4 ± 0.3atmN/ATsonopoulos and Ambrose, 1996 
Pc45.19atmN/AOhgaki, Umezono, et al., 1990Uncertainty assigned by TRC = 0.15 atm; TRC
Pc46.036atmN/AAngus, Armstrong, et al., 1980Uncertainty assigned by TRC = 1.97 atm; TRC
Pc45.61atmN/AMarchman, Prengle, et al., 1949Uncertainty assigned by TRC = 0.1499 atm; TRC
Pc45.3460atmN/ASeibert and Burrell, 1915Uncertainty assigned by TRC = 0.3289 atm; TRC
Quantity Value Units Method Reference Comment
Vc0.1846l/molN/ATsonopoulos and Ambrose, 1996 
Vc0.192l/molN/AMarchman, Prengle, et al., 1949Uncertainty assigned by TRC = 0.005 l/mol; TRC
Quantity Value Units Method Reference Comment
ρc5.42 ± 0.03mol/lN/ATsonopoulos and Ambrose, 1996 
ρc5.549mol/lN/AOhgaki, Umezono, et al., 1990Uncertainty assigned by TRC = 0.07 mol/l; TRC
ρc5.309mol/lN/AAngus, Armstrong, et al., 1980Uncertainty assigned by TRC = 0.36 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap3.834kcal/molN/AMajer and Svoboda, 1985 

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
4.402225.5N/AMajer and Svoboda, 1985 
4.4020225.35N/APowell and Giauque, 1939DH
4.47312.AStephenson and Malanowski, 1987Based on data from 297. to 363. K.; AC
5.31146.AStephenson and Malanowski, 1987Based on data from 104. to 161. K.; AC
4.47256.AStephenson and Malanowski, 1987Based on data from 228. to 271. K.; AC
4.42285.AStephenson and Malanowski, 1987Based on data from 270. to 327. K.; AC
4.49340.AStephenson and Malanowski, 1987Based on data from 325. to 363. K.; AC
4.59227.AStephenson and Malanowski, 1987Based on data from 161. to 242. K. See also Dykyj, 1970.; AC
4.47360.N/AMichels, Wassenaar, et al., 1953Based on data from 298. to 423. K.; AC
4.68211.N/APowell and Giauque, 1939Based on data from 166. to 226. K.; AC
4.61268.N/AMaass and Wright, 1921Based on data from 236. to 283. K. See also Boublik, Fried, et al., 1984.; AC

Entropy of vaporization

ΔvapS (cal/mol*K) Temperature (K) Reference Comment
19.53225.35Powell and Giauque, 1939DH

Antoine Equation Parameters

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

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Temperature (K) A B C Reference Comment
165.81 to 225.983.96917795.819-24.884Powell and Giauque, 1939Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
0.717787.85Chao, Hall, et al., 1983DH
0.717587.85Powell and Giauque, 1939DH
0.701088.2Huffman, Parks, et al., 1931DH
0.70088.2Domalski and Hearing, 1996AC

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
8.16987.85Chao, Hall, et al., 1983DH
8.16987.85Powell and Giauque, 1939DH
7.9688.2Huffman, Parks, et al., 1931DH

Temperature of phase transition

Ttrs (K) Initial Phase Final Phase Reference Comment
56.0crystalineglassTakeda, Oguni, et al., 1990DH

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:


Henry's Law data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Gas phase ion energetics data, 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: Rolf Sander

Henry's Law constant (water solution)

kH(T) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference Comment
0.0048 QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
0.0048 LN/A 
0.00743400.LN/A 
0.0048 VN/A 

Gas phase ion energetics data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, References, Notes

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

Data evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias

Data compiled as indicated in comments:
B - John E. Bartmess
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron

View reactions leading to C3H6+ (ion structure unspecified)

Quantity Value Units Method Reference Comment
IE (evaluated)9.73 ± 0.01eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)179.6kcal/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity172.7kcal/molN/AHunter and Lias, 1998HL

Ionization energy determinations

IE (eV) Method Reference Comment
9.73PITraeger, 1984LBLHLM
9.69 ± 0.09EISelim, 1980LLK
9.73 ± 0.02PIWood and Taylor, 1979LLK
9.7 ± 0.1PEBieri, Burger, et al., 1977LLK
9.73 ± 0.01PIKrassig, Reinke, et al., 1974LLK
9.744 ± 0.003PEMasclet, Grosjean, et al., 1973LLK
9.72PEKatrib and Rabalais, 1973LLK
9.72EILossing, 1972LLK
9.74PEFrost and Sandhu, 1971LLK
9.74 ± 0.01PIPerson and Nicole, 1970RDSH
9.69PEDewar and Worley, 1969RDSH
9.76CICermak, 1968RDSH
9.727 ± 0.010PINicholson, 1965RDSH
9.74SSamson, Marmo, et al., 1962RDSH
9.73 ± 0.02PISteiner, Giese, et al., 1961RDSH
9.73PIBralsford, Harris, et al., 1960RDSH
9.73 ± 0.01PIWatanabe, 1957RDSH
9.91 ± 0.01PEKrause, Taylor, et al., 1978Vertical value; LLK
10.2PEKobayashi, 1978Vertical value; LLK
10.03PEKimura, Katsumata, et al., 1975Vertical value; LLK
10.2PEWhite, Carlson, et al., 1974Vertical value; LLK
9.70PEHentrich, Gunkel, et al., 1974Vertical value; LLK
9.9PEWeidner and Schweig, 1972Vertical value; LLK
9.86PEMollere, Bock, et al., 1972Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
C+24.5 ± 0.5?EIPeers and Vigny, 1968RDSH
CH+22.5 ± 0.5?EIPeers and Vigny, 1968RDSH
CH2+17.0 ± 0.5?EIPeers and Vigny, 1968RDSH
CH3+14.9C2H3EIHaney and Franklin, 1968RDSH
CH4+14.7 ± 0.5?EIPeers and Vigny, 1968RDSH
C2+28. ± 1.?EIPeers and Vigny, 1968RDSH
C2H+21. ± 1.?EIPeers and Vigny, 1968RDSH
C2H2+12.92 ± 0.05CH4PIKrassig, Reinke, et al., 1974LLK
C2H2+13.6 ± 0.5CH4EIPeers and Vigny, 1968RDSH
C2H2+14.1CH4EIHaney and Franklin, 1968RDSH
C2H3+13.78 ± 0.03CH3EISelim, 1980LLK
C2H3+13.20 ± 0.04CH3PIKrassig, Reinke, et al., 1974LLK
C2H3+13.7 ± 0.5CH3EIPeers and Vigny, 1968RDSH
C2H4+12.4 ± 0.5?EIPeers and Vigny, 1968RDSH
C2H5+12.6 ± 0.5?EIPeers and Vigny, 1968RDSH
C3+27. ± 1.?EIPeers and Vigny, 1968RDSH
C3H+20.5 ± 0.52H2+HEIPeers and Vigny, 1968RDSH
C3H+20.2 ± 0.52H2+HEIHarrison and Tait, 1962RDSH
C3H2+47. ± 1.?EIPeers and Vigny, 1968RDSH
C3H2+17. ± 1.2H2EIPeers and Vigny, 1968RDSH
C3H3+14.21 ± 0.09H2+HEISelim, 1980LLK
C3H3+13.19 ± 0.05H2+HPIKrassig, Reinke, et al., 1974LLK
C3H3+14.3 ± 0.5H2+HEIPeers and Vigny, 1968RDSH
C3H3+14.21H2+HEIOmura, 1962RDSH
C3H4+11.91 ± 0.03H2PIKrassig, Reinke, et al., 1974LLK
C3H4+12.3 ± 0.5H2EIPeers and Vigny, 1968RDSH
C3H4+12.52H2EIOmura, 1961RDSH
C3H5+11.86HPITraeger, 1984LBLHLM
C3H5+11.90 ± 0.05HEISelim, 1980LLK
C3H5+11.78HPIButtrill, Williamson, et al., 1975LLK
C3H5+11.88 ± 0.03HPIKrassig, Reinke, et al., 1974LLK
C3H5+11.88HEILossing, 1971LLK
C3H22+33.3 ± 0.5?EIPeers and Vigny, 1968RDSH
C3H52+31.1 ± 0.5HEIPeers and Vigny, 1968RDSH
H+20. ± 1.?EIPeers and Vigny, 1968RDSH
H2+16. ± 1.?EIPeers and Vigny, 1968RDSH

De-protonation reactions

C3H5- + Hydrogen cation = Propene

By formula: C3H5- + H+ = C3H6

Quantity Value Units Method Reference Comment
Δr391.10 ± 0.30kcal/molG+TSEllison, Davico, et al., 1996gas phase; calculated dSacid=24.2±1.0 eu; B
Δr390.5 ± 1.0kcal/molD-EAWenthold, Polak, et al., 1996gas phase; B
Δr390.7 ± 2.1kcal/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr390.25 ± 0.65kcal/molG+TSMackay, Lien, et al., 1978gas phase; B
Quantity Value Units Method Reference Comment
Δr383.80 ± 0.10kcal/molIMREEllison, Davico, et al., 1996gas phase; calculated dSacid=24.2±1.0 eu; B
Δr383.9 ± 1.1kcal/molH-TSWenthold, Polak, et al., 1996gas phase; B
Δr384.1 ± 2.0kcal/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr383.60 ± 0.50kcal/molIMREMackay, Lien, et al., 1978gas phase; B

C3H5- + Hydrogen cation = Propene

By formula: C3H5- + H+ = C3H6

Quantity Value Units Method Reference Comment
Δr405.8 ± 2.0kcal/molBranDePuy, Gronert, et al., 1989gas phase; B
Δr>404.75 ± 0.60kcal/molG+TSFroelicher, Freiser, et al., 1986gas phase; B
Quantity Value Units Method Reference Comment
Δr398.0 ± 2.1kcal/molH-TSDePuy, Gronert, et al., 1989gas phase; B
Δr>397.00kcal/molIMRBFroelicher, Freiser, et al., 1986gas phase; B

C3H5- + Hydrogen cation = Propene

By formula: C3H5- + H+ = C3H6

Quantity Value Units Method Reference Comment
Δr>404.75 ± 0.90kcal/molG+TSFroelicher, Freiser, et al., 1986gas phase; B
Quantity Value Units Method Reference Comment
Δr>397.00kcal/molIMRBFroelicher, Freiser, et al., 1986gas phase; B

References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Notes

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

Furuyama, Golden, et al., 1969
Furuyama, S.; Golden, D.M.; Benson, S.W., Thermochemistry of the gas phase equilibria i-C3H7I = C3H6 + HI, n-C3H7I = i-C3H7I, and C3H6 + 2HI = C3H8 + I2, J. Chem. Thermodyn., 1969, 1, 363-375. [all data]

Lacher, Walden, et al., 1950
Lacher, J.R.; Walden, C.H.; Lea, K.R.; Park, J.D., Vapor phase heats of hydrobromination of cyclopropane and propylene, J. Am. Chem. Soc., 1950, 72, 331-333. [all data]

Wiberg and Fenoglio, 1968
Wiberg, K.B.; Fenoglio, R.A., Heats of formation of C4H6 hydrocarbons, J. Am. Chem. Soc., 1968, 90, 3395-3397. [all data]

Rossini and Knowlton, 1937
Rossini, F.d.; Knowlton, J.W., Calorimetric determination of the heats of combustion of ethylene and propylene, J. Res. NBS, 1937, 19, 249-262. [all data]

Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G., Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]

Thermodynamics Research Center, 1997
Thermodynamics Research Center, Selected Values of Properties of Chemical Compounds., Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1997. [all data]

Crawford B.L., 1939
Crawford B.L., Jr., The entropy and heat capacity of propylene, J. Am. Chem. Soc., 1939, 61, 2980-2981. [all data]

Kilpatrick J.E., 1946
Kilpatrick J.E., Heat content, free energy function, entropy, and heat capacity of ethylene, propylene, and the four butenes to 1500 K, J. Res. Nat. Bur. Stand, 1946, 37, 163-171. [all data]

Kilpatrick J.E., 1947
Kilpatrick J.E., Normal coordinate analysis of the vibrational frequencies of ethylene, propylene, cis-2-butene, trans-2-butene, and isobutene, J. Res. Nat. Bur. Stand., 1947, 38, 191-209. [all data]

Chao J., 1975
Chao J., Ideal gas thermodynamic properties of ethylene and propylene, J. Phys. Chem. Ref. Data, 1975, 4, 251-261. [all data]

East A.L.L., 1997
East A.L.L., Ab initio statistical thermodynamical models for the computation of third-law entropies, J. Chem. Phys., 1997, 106, 6655-6674. [all data]

Bier K., 1974
Bier K., Thermodynamic properties of propylene from calorimetric measurements, J. Chem. Thermodyn., 1974, 6, 1039-1052. [all data]

Kistiakowsky G.B., 1940
Kistiakowsky G.B., The low temperature gaseous heat capacities of certain C3 hydrocarbons, J. Chem. Phys., 1940, 8, 970-977. [all data]

Kistiakowsky G.B., 1940, 2
Kistiakowsky G.B., Gaseous heat capacities. II, J. Chem. Phys., 1940, 8, 610-618. [all data]

Telfair D., 1942
Telfair D., Supersonic measurement of the heat capacity of propylene, J. Chem. Phys., 1942, 10, 167-171. [all data]

Chao, Hall, et al., 1983
Chao, J.; Hall, K.R.; Yao, J.M., Thermodynamic properties of simple alkenes, Thermochim. Acta, 1983, 64(3), 285-303. [all data]

Auerbach, Sage, et al., 1950
Auerbach, C.E.; Sage, B.H.; Lacey, W.N., Isobaric heat capacities at bubble point, Ind. Eng. Chem., 1950, 42, 110-113. [all data]

Powell and Giauque, 1939
Powell, T.M.; Giauque, W.F., Propylene. The heat capacity, vapor pressure, heats of fusion and vaporization. The third law of thermodynamics and orientation equilibrium in the solid, J. Am. Chem. Soc., 1939, 61, 2366-2370. [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]

Streng, 1971
Streng, A.G., Miscibility and Compatibility of Some Liquid and Solidified Gases at Low Temperature, J. Chem. Eng. Data, 1971, 16, 357. [all data]

Haselden and Snowden, 1962
Haselden, G.G.; Snowden, P., Equilibrium Properties of the Carbon Dioxide+ Propylene and Carbon Dioxide + Cyclopropane Systems at Low Temperatures, Trans. Faraday Soc., 1962, 58, 1515-28. [all data]

Parks and Huffman, 1931
Parks, G.S.; Huffman, H.M., Some fusion and transition data for hydrocarbons, Ind. Eng. Chem., 1931, 23, 1138-9. [all data]

Coffin and Maass, 1927
Coffin, C.C.; Maass, O., The Prepartion and Physical Properties of Isobutylene, Trans. R. Soc. Can., Sect. 3, 1927, 21, 33. [all data]

Angus, Armstrong, et al., 1980
Angus, S.; Armstrong, B.; de Reuck, K.M., International Thermodynamic Tables of the Fluid State - 7 Propylene(Propene), Pergamon, New York, 1980. [all data]

Tsonopoulos and Ambrose, 1996
Tsonopoulos, C.; Ambrose, D., Vapor-Liquid Critical Properties of Elements and Compounds. 6. Unsaturated Aliphatic Hydrocarbons, J. Chem. Eng. Data, 1996, 41, 645-656. [all data]

Ohgaki, Umezono, et al., 1990
Ohgaki, K.; Umezono, S.; Katayama, T., Pressure-density-temperature (p-ρ-T) relations of fluoroform, nitrous oxide, and propene in the critical region, J. Supercrit. Fluids, 1990, 3, 78-84. [all data]

Marchman, Prengle, et al., 1949
Marchman, H.; Prengle, H.W.; Motard, R.L., Compressibility and Critical Constants of Propylene Vapor, Ind. Eng. Chem., 1949, 41, 2658. [all data]

Seibert and Burrell, 1915
Seibert, F.M.; Burrell, G.A., The Critical Constants of Normal Butane, Iso-butane and Propylene and Their Vapor Pressures at Temperatures Bewtween 0 deg.C and 120 deg.C, J. Am. Chem. Soc., 1915, 37, 2683-91. [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]

Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw, Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2 . [all data]

Dykyj, 1970
Dykyj, J., Petrochemica, 1970, 10, 2, 51. [all data]

Michels, Wassenaar, et al., 1953
Michels, A.; Wassenaar, T.; Louwerse, P.; Lunbeck, R.J.; Wolkers, G.J., Isotherms and thermodynamical functions of propene at temperatures between 25° and 150°c and at densities up to 340 amagat (pressures up to 2800 atm), Physica, 1953, 19, 1-12, 287-297, https://doi.org/10.1016/S0031-8914(53)80030-3 . [all data]

Maass and Wright, 1921
Maass, O.; Wright, C.H., SOME PHYSICAL PROPERTIES OF HYDROCARBONS CONTAINING TWO AND THREE CARBON ATOMS., J. Am. Chem. Soc., 1921, 43, 5, 1098-1111, https://doi.org/10.1021/ja01438a013 . [all data]

Boublik, Fried, et al., 1984
Boublik, T.; Fried, V.; Hala, E., The Vapour Pressures of Pure Substances: Selected Values of the Temperature Dependence of the Vapour Pressures of Some Pure Substances in the Normal and Low Pressure Region, 2nd ed., Elsevier, New York, 1984, 972. [all data]

Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D., Heat Capacities and Entropies of Organic Compounds in the Condensed Phase. Volume III, J. Phys. Chem. Ref. Data, 1996, 25, 1, 1, https://doi.org/10.1063/1.555985 . [all data]

Takeda, Oguni, et al., 1990
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Notes

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