Propene

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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 - 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, 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 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

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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 - 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. - 363. K.; AC
5.31146.AStephenson and Malanowski, 1987Based on data from 104. - 161. K.; AC
4.47256.AStephenson and Malanowski, 1987Based on data from 228. - 271. K.; AC
4.42285.AStephenson and Malanowski, 1987Based on data from 270. - 327. K.; AC
4.49340.AStephenson and Malanowski, 1987Based on data from 325. - 363. K.; AC
4.59227.AStephenson and Malanowski, 1987Based on data from 161. - 242. K. See also Dykyj, 1970.; AC
4.47360.N/AMichels, Wassenaar, et al., 1953Based on data from 298. - 423. K.; AC
4.68211.N/APowell and Giauque, 1939Based on data from 166. - 226. K.; AC
4.61268.N/AMaass and Wright, 1921Based on data from 236. - 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 - 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:


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:
B - John E. Bartmess
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
RCD - Robert C. Dunbar

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

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

Hydrogen bromide + Propene = Propane, 2-bromo-

By formula: HBr + C3H6 = C3H7Br

Quantity Value Units Method Reference Comment
Δr-20.43kcal/molCmLacher, Kianpour, et al., 1957gas phase; ALS
Δr-20.050kcal/molCmLacher, Lea, et al., 1950gas phase; Heat of hydrobromination at 367°K; ALS
Δr-20.10 ± 0.14kcal/molCmLacher, Walden, et al., 1950gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -20.17 ± 0.24 kcal/mol; Heat of hydrobromination; ALS

Propene + Hydrogen = Propane

By formula: C3H6 + H2 = C3H8

Quantity Value Units Method Reference Comment
Δr-29.5 ± 1.2kcal/molChydKistiakowsky and Nickle, 1951gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -29.85 ± 0.50 kcal/mol; ALS
Δr-29.87 ± 0.10kcal/molChydKistiakowsky, Ruhoff, et al., 1935gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -30.115 ± 0.013 kcal/mol; At 355 °K; ALS

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

Hydrogen iodide + 1-Propene, 3-iodo- = Propene + Iodine

By formula: HI + C3H5I = C3H6 + I2

Quantity Value Units Method Reference Comment
Δr-7.96 ± 0.33kcal/molEqkRodgers, Golden, et al., 1966gas phase; ALS
Δr-9.5 ± 1.0kcal/molEqkRodgers, Golden, et al., 1966gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -8.33 ± 0.23 kcal/mol; At 527 K; ALS

Propane, 2-chloro- = Propene + Hydrogen chloride

By formula: C3H7Cl = C3H6 + HCl

Quantity Value Units Method Reference Comment
Δr17.3 ± 0.2kcal/molEqkNoren and Sunner, 1970gas phase; ALS
Δr17.62 ± 0.15kcal/molEqkKabo and Andreevskii, 1963gas phase; At 415.5 K; ALS
Δr17.45 ± 0.50kcal/molEqkHowlett, 1955gas phase; ALS

Cobalt ion (1+) + Propene = (Cobalt ion (1+) • Propene)

By formula: Co+ + C3H6 = (Co+ • C3H6)

Enthalpy of reaction

ΔrH° (kcal/mol) T (K) Method Reference Comment
43.0 (+1.7,-0.) CIDArmentrout and Kickel, 1994gas phase; guided ion beam CID; M
43.1 (+1.6,-0.) CIDHaynes and Armentrout, 1994gas phase; guided ion beam CID; M

C3H9Si+ + Propene = (C3H9Si+ • Propene)

By formula: C3H9Si+ + C3H6 = (C3H9Si+ • C3H6)

Quantity Value Units Method Reference Comment
Δr30.6kcal/molPHPMSLi and Stone, 1989gas phase; condensation; M
Quantity Value Units Method Reference Comment
Δr42.5cal/mol*KPHPMSLi and Stone, 1989gas phase; condensation; M

Propene + Bromine = Propane, 1,2-dibromo-

By formula: C3H6 + Br2 = C3H6Br2

Quantity Value Units Method Reference Comment
Δr-29.27 ± 0.20kcal/molCmConn, Kistiakowsky, et al., 1938gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -29.41 ± 0.20 kcal/mol; At 355 °K; ALS

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

Lithium ion (1+) + Propene = (Lithium ion (1+) • Propene)

By formula: Li+ + C3H6 = (Li+ • C3H6)

Quantity Value Units Method Reference Comment
Δr23.kcal/molICRStaley and Beauchamp, 1975gas phase; switching reaction(Li+)H2O, from graph; Dzidic and Kebarle, 1970 extrapolated; M

Rh+ + Propene = (Rh+ • Propene)

By formula: Rh+ + C3H6 = (Rh+ • C3H6)

Enthalpy of reaction

ΔrH° (kcal/mol) T (K) Method Reference Comment
28.1 CIDChen and Armetrout, 1995gas phase; ΔrH>=, guided ion beam CID; M

Iron ion (1+) + Propene = (Iron ion (1+) • Propene)

By formula: Fe+ + C3H6 = (Fe+ • C3H6)

Enthalpy of reaction

ΔrH° (kcal/mol) T (K) Method Reference Comment
34.7 (+1.7,-0.) CIDArmentrout and Kickel, 1994gas phase; guided ion beam CID; M

(CAS Reg. No. 25012-80-0 • 4294967295Propene) + Propene = CAS Reg. No. 25012-80-0

By formula: (CAS Reg. No. 25012-80-0 • 4294967295C3H6) + C3H6 = CAS Reg. No. 25012-80-0

Quantity Value Units Method Reference Comment
Δr10.8 ± 2.1kcal/molN/ADePuy, Gronert, et al., 1989gas phase; B

(CAS Reg. No. 59513-13-2 • 4294967295Propene) + Propene = CAS Reg. No. 59513-13-2

By formula: (CAS Reg. No. 59513-13-2 • 4294967295C3H6) + C3H6 = CAS Reg. No. 59513-13-2

Quantity Value Units Method Reference Comment
Δr14.6 ± 2.1kcal/molN/ADePuy, Gronert, et al., 1989gas phase; B

Propene + Hydrogen chloride = Propane, 2-chloro-

By formula: C3H6 + HCl = C3H7Cl

Quantity Value Units Method Reference Comment
Δr-17.54kcal/molEqkKabo and Andreevskii, 1963gas phase; At 385°K; ALS

Hydrogen iodide + Propene = Propane, 2-iodo-

By formula: HI + C3H6 = C3H7I

Quantity Value Units Method Reference Comment
Δr-20.62kcal/molEqkFuruyama, Golden, et al., 1969gas phase; ALS

Propene + Sulfuric Acid = isopropyl hydrogen sulphate

By formula: C3H6 + H2O4S = isopropyl hydrogen sulphate

Quantity Value Units Method Reference Comment
Δr-9.2 ± 0.2kcal/molEqkEntelis, Korovina, et al., 1960liquid phase; ALS

1,2-Diiodopropane = Propene + Iodine

By formula: C3H6I2 = C3H6 + I2

Quantity Value Units Method Reference Comment
Δr11.2 ± 0.4kcal/molEqkBenson and Amano, 1962gas phase; ALS

Propane, 2-bromo- = Hydrogen bromide + Propene

By formula: C3H7Br = HBr + C3H6

Quantity Value Units Method Reference Comment
Δr19.3 ± 0.5kcal/molEqkRozhnov and Andreevskii, 1962gas phase; ALS

Propene + 2-Propanone, 1,1,1,3,3,3-hexafluoro- = 4-Penten-2-ol, 1,1,1-trifluoro-2-(trifluoromethyl)-

By formula: C3H6 + C3F6O = C6H6F6O

Quantity Value Units Method Reference Comment
Δr-18.7 ± 1.0kcal/molEqkMoore, 1971gas phase; ALS

Gold ion (1+) + Propene = (Gold ion (1+) • Propene)

By formula: Au+ + C3H6 = (Au+ • C3H6)

Quantity Value Units Method Reference Comment
Δr>75.kcal/molIMRBSchroeder, Hrusak, et al., 1995RCD

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 Spectrometry Data Center, William E. Wallace, 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 Spectrometry Data Center, William E. Wallace, director

Spectrum

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NIST MS number 50

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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.

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]

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Notes

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