1-Pentene
- Formula: C5H10
- Molecular weight: 70.1329
- IUPAC Standard InChIKey: YWAKXRMUMFPDSH-UHFFFAOYSA-N
- CAS Registry Number: 109-67-1
- Chemical structure:
This structure is also available as a 2d Mol file or as a computed 3d SD file
The 3d structure may be viewed using Java or Javascript. - Other names: α-n-Amylene; Propylethylene; 1-C5H10; Pent-1-ene; 1-Pentene 95; Pentene-1
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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 compiled as indicated in comments:
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -5. ± 2. | kcal/mol | AVG | N/A | Average of 6 values; Individual data points |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
19.68 | 200. | Thermodynamics Research Center, 1997 | p=1 bar. Recommended values were calculated from data for lower alkenes by a method of increments. These values are in good agreement with experimental data. The results of the similar estimation [ Kilpatrick J.E., 1946] are in poor agreement with experiment.; GT |
24.19 | 273.15 | ||
25.86 | 298.15 | ||
25.98 | 300. | ||
32.89 | 400. | ||
39.20 | 500. | ||
44.53 | 600. | ||
49.02 | 700. | ||
52.82 | 800. | ||
56.07 | 900. | ||
58.84 | 1000. | ||
61.28 | 1100. | ||
63.36 | 1200. | ||
65.20 | 1300. | ||
66.73 | 1400. | ||
68.21 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
26.850 ± 0.079 | 311.09 | Scott D.W., 1949 | GT |
30.151 ± 0.091 | 357.51 | ||
33.24 ± 0.10 | 402.32 | ||
35.47 ± 0.11 | 436.01 | ||
37.69 ± 0.11 | 471.08 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry 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 compiled as indicated in comments:
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -12. ± 1. | kcal/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -800.60 ± 0.14 | kcal/mol | Ccb | Good and Smith, 1979 | Corresponding ΔfHºliquid = -11.23 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 62.763 | cal/mol*K | N/A | Messerly, Todd, et al., 1990 | DH |
S°liquid | 62.76 | cal/mol*K | N/A | Chao, Hall, et al., 1983 | DH |
S°liquid | 62.751 | cal/mol*K | N/A | Todd, Oliver, et al., 1947 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
37.015 | 298.15 | Messerly, Todd, et al., 1990 | T = 10 to 320 K.; DH |
36.8 | 298.15 | Chao, Hall, et al., 1983 | T = 12 to 353 K.; DH |
36.88 | 294. | Schlinger and Sage, 1949 | T = 294 to 378 K. Cp given as 0.526 Btu/lb*R at 70°F.; DH |
37.120 | 298.15 | Todd, Oliver, et al., 1947 | T = 12 to 300 K.; 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 - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 304. ± 8. | K | AVG | N/A | Average of 30 out of 31 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 107.75 | K | N/A | Streiff, Murphy, et al., 1946 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tfus | 107.78 | K | N/A | Streiff, Murphy, et al., 1946 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tfus | 107.88 | K | N/A | Streiff, Murphy, et al., 1946 | Uncertainty assigned by TRC = 0.1 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 108.010 | K | N/A | Messerly, Todd, et al., 1990, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.003 K; TRC |
Ttriple | 107.790 | K | N/A | Messerly, Todd, et al., 1990, 2 | Metastable crystal phase; Uncertainty assigned by TRC = 0.003 K; TRC |
Ttriple | 5.800 | K | N/A | Chao, Hall, et al., 1983, 2 | Uncertainty assigned by TRC = 0.01 K; TRC |
Ttriple | 107.9 | K | N/A | Todd, Oliver, et al., 1947, 2 | Uncertainty assigned by TRC = 0.5 K; this value not measured but taken from 1956-strmur 0; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 464.8 ± 0.5 | K | N/A | Tsonopoulos and Ambrose, 1996 | |
Tc | 464.7 | K | N/A | Majer and Svoboda, 1985 | |
Tc | 465.1 | K | N/A | Wolfe, Kay, et al., 1983 | Uncertainty assigned by TRC = 0.3 K; $ %Y/SI 0.01 @Y/SI 0.3; TRC |
Tc | 463.77 | K | N/A | Mousa, Kay, et al., 1972 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tc | 464.74 | K | N/A | Ambrose, Cox, et al., 1960 | Uncertainty assigned by TRC = 0.03 K; Visual, PRT, IPTS-48; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 35.1 ± 0.5 | atm | N/A | Tsonopoulos and Ambrose, 1996 | |
Pc | 35.04 | atm | N/A | Wolfe, Kay, et al., 1983 | Uncertainty assigned by TRC = 0.20 atm; $ %Y/SI 1.5 @Y/SI 20.; TRC |
Pc | 35.046 | atm | N/A | Mousa, Kay, et al., 1972 | Uncertainty assigned by TRC = 0.0340 atm; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.2984 | l/mol | N/A | Tsonopoulos and Ambrose, 1996 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.35 ± 0.05 | mol/l | N/A | Tsonopoulos and Ambrose, 1996 | |
ρc | 3.32 | mol/l | N/A | Wolfe, Kay, et al., 1983 | Uncertainty assigned by TRC = 0.03 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 7.127 | kcal/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 6.09 | kcal/mol | N/A | Reid, 1972 | AC |
ΔvapH° | 6.09 ± 0.02 | kcal/mol | C | Scott, Waddington, et al., 1949 | AC |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
6.02 | 303.1 | N/A | Majer and Svoboda, 1985 | |
6.96 | 233. | A | Stephenson and Malanowski, 1987 | Based on data from 218. to 311. K.; AC |
6.38 | 295. | MM | Forziati, Camin, et al., 1950 | Based on data from 286. to 304. K.; AC |
6.43 | 288. | N/A | Scott, Waddington, et al., 1949 | Based on data from 273. to 334. K.; AC |
6.26 ± 0.02 | 284. | C | Scott, Waddington, et al., 1949 | AC |
6.02 ± 0.02 | 303. | C | Scott, Waddington, et al., 1949 | AC |
6.29 | 290. | N/A | Day, Nicholson, et al., 1948 | Based on data from 273. to 308. K.; AC |
6.14 | 341. | N/A | Day, Nicholson, et al., 1948 | Based on data from 313. to 368. K.; AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kcal/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | A (kcal/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
284. to 303. | 9.491 | 0.2663 | 464.7 | Majer and Svoboda, 1985 |
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 |
---|---|---|---|---|
285.98 to 303.87 | 3.90487 | 1014.294 | -43.367 | Forziati, Camin, et al., 1950, 2 |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
1.41907 | 108.016 | Messerly, Todd, et al., 1990 | DH |
1.40576 | 107.797 | Messerly, Todd, et al., 1990 | c(metastable)/liq; DH |
1.388 | 107.90 | Chao, Hall, et al., 1983 | DH |
1.388 | 107.9 | Todd, Oliver, et al., 1947 | DH |
1.39 | 107.9 | Acree, 1991 | See also Messerly, Todd, et al., 1990.; AC |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
13.14 | 108.016 | Messerly, Todd, et al., 1990 | DH |
13.04 | 107.797 | Messerly, Todd, et al., 1990 | c(metastable)/liq; DH |
12.86 | 107.90 | Chao, Hall, et al., 1983 | DH |
12.86 | 107.9 | Todd, Oliver, et al., 1947 | DH |
Temperature of phase transition
Ttrs (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|
71.7 | crystaline | glass | Takeda, Oguni, et al., 1990 | DH |
Reaction thermochemistry 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 compiled by: Hussein Y. Afeefy, Joel F. Liebman, and Stephen 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
By formula: C5H10 + H2 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -30.27 ± 0.58 | kcal/mol | Chyd | Molnar, Rachford, et al., 1984 | liquid phase; solvent: Dioxane |
ΔrH° | -29.87 ± 0.42 | kcal/mol | Chyd | Molnar, Rachford, et al., 1984 | liquid phase; solvent: Hexane |
ΔrH° | -29.30 ± 0.57 | kcal/mol | Chyd | Rogers and Skanupong, 1974 | liquid phase; solvent: Hexane |
ΔrH° | -28.5 ± 0.3 | kcal/mol | Chyd | Rogers and McLafferty, 1971 | liquid phase; solvent: Hydrocarbon |
By formula: C5H10 = C5H10
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -2.6 ± 0.2 | kcal/mol | Eqk | Egger and Benson, 1966 | gas phase; Heat of Isomerization |
By formula: C5H11Cl = C5H10 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 17.6 | kcal/mol | Eqk | Karaseva and Andreevskii, 1969 | gas phase |
Henry's Law 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 by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
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)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference | Comment |
---|---|---|---|---|
0.0025 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.0025 | L | N/A | ||
0.0025 | V | N/A |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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]
Kilpatrick J.E., 1946
Kilpatrick J.E.,
Heats, equilibrium constants, and free energies of formation of the monoolefin hydrocarbons,
J. Res. Nat. Bur. Stand, 1946, 36, 559-612. [all data]
Scott D.W., 1949
Scott D.W.,
Thermodynamic properties of three isomeric pentenes,
J. Am. Chem. Soc., 1949, 71, 2767-2773. [all data]
Good and Smith, 1979
Good, W.D.; Smith, N.K.,
The enthalpies of combustion of the isomeric pentenes in the liquid state. A warning to combustion calorimetrists about sample drying,
J. Chem. Thermodyn., 1979, 11, 111-118. [all data]
Messerly, Todd, et al., 1990
Messerly, J.F.; Todd, S.S.; Finke, H.L.; Lee-Bechtold, S.H.; Guthrie, G.B.; Steele, W.V.; Chirico, R.D.,
Heat capacities of pent-1-ene (10K to 320K), cis-hex-2-ene (10K to 330K), non-1-ene (10K to 400K), and hexadec-1-ene (10K to 400K),
J. Chem. Thermodynam., 1990, 22, 1107-1128. [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]
Todd, Oliver, et al., 1947
Todd, S.S.; Oliver, G.D.; Huffman, H.M.,
The heat capacities, heats of fusion and entropies of the six pentenes,
J. Am. Chem. Soc., 1947, 69, 1519-1525. [all data]
Schlinger and Sage, 1949
Schlinger, W.G.; Sage, B.H.,
Isobaric heat capacity of 1-butene and 1-pentene at bubble point,
Ind. Eng. Chem., 1949, 41, 1779-1782. [all data]
Streiff, Murphy, et al., 1946
Streiff, A.J.; Murphy, E.T.; Sedlak, V.A.; Willingham, C.B.; Rossini, F.D.,
Purification, Purity, and Freezing Points of 7 Heptanes, 16 Octanes, 6 Pentene, Cyclopentene, and 7 C9H12 Alkylbenzenes of the API-Standard and API-NBS Series,
J. Res. Natl. Bur. Stand. (U. S.), 1946, 37, 331. [all data]
Messerly, Todd, et al., 1990, 2
Messerly, J.F.; Todd, S.S.; Finke, H.L.; Lee-Bechtold, S.H.; Guthrie, G.B.; Steele, W.V.; Chirico, R.D.,
Heat capacities of pent-1-ene (10 K to 320 K), cis-hex-2-ene (10 K to 330 K), non-1-ene (10 K to 400 K) and hexadec-1-ene (10 K to 400 K),
J. Chem. Thermodyn., 1990, 22, 1107-28. [all data]
Chao, Hall, et al., 1983, 2
Chao, J.; Hall, K.R.; Yao, J.M.,
Thermodynamic Properties of Simple Alkenes,
Thermochim. Acta, 1983, 64, 285. [all data]
Todd, Oliver, et al., 1947, 2
Todd, S.S.; Oliver, G.D.; Huffman, H.M.,
The heat capacities, heats of fusion and entropies of the six pentenes.,
J. Am. Chem. Soc., 1947, 69, 1519. [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]
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]
Wolfe, Kay, et al., 1983
Wolfe, D.; Kay, W.B.; Teja, A.S.,
Phase Equilibria in the n-Pentane + Pent-1-ene System 1. Critical States,
J. Chem. Eng. Data, 1983, 28, 319. [all data]
Mousa, Kay, et al., 1972
Mousa, A.H.N.; Kay, W.B.; Kreglewski, A.,
The critical constants of binary mixtures of certain perfluoro-compounds with alkanes,
J. Chem. Thermodyn., 1972, 4, 301-11. [all data]
Ambrose, Cox, et al., 1960
Ambrose, D.; Cox, J.D.; Townsend, R.,
The critical temperatures of forty organic compounds,
Trans. Faraday Soc., 1960, 56, 1452. [all data]
Reid, 1972
Reid, Robert C.,
Handbook on vapor pressure and heats of vaporization of hydrocarbons and related compounds, R. C. Wilhort and B. J. Zwolinski, Texas A Research Foundation. College Station, Texas(1971). 329 pages.$10.00,
AIChE J., 1972, 18, 6, 1278-1278, https://doi.org/10.1002/aic.690180637
. [all data]
Scott, Waddington, et al., 1949
Scott, D.W.; Waddington, G.; Smith, J.C.; Huffman, H.M.,
Thermodynamic properties of three isomeric pentenes,
J. Am. Chem. Soc., 1949, 71, 2767-2773. [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]
Forziati, Camin, et al., 1950
Forziati, A.F.; Camin, D.L.; Rossini, F.D.,
Density, refractive index, boiling point, and vapor pressure of eight monoolefin (1-alkene), six pentadiene, and two cyclomonoolefin hydrocarbons,
J. RES. NATL. BUR. STAN., 1950, 45, 5, 406, https://doi.org/10.6028/jres.045.044
. [all data]
Day, Nicholson, et al., 1948
Day, H.O.; Nicholson, D.E.; Felsing, W.A.,
The Vapor Pressures and Some Related Quantities of Pentene-1 from 0 to 200°,
J. Am. Chem. Soc., 1948, 70, 5, 1784-1785, https://doi.org/10.1021/ja01185a037
. [all data]
Forziati, Camin, et al., 1950, 2
Forziati, a.F.; Camin, D.L.; Rossini, F.D.,
Density, refractive index, boiling point, and vapor pressure of eight monoolefin (1-alkene), six pentadiene, and two cyclomonoolefin hydrocarbons,
J. Res. NBS, 1950, 45, 406-410. [all data]
Acree, 1991
Acree, William E.,
Thermodynamic properties of organic compounds: enthalpy of fusion and melting point temperature compilation,
Thermochimica Acta, 1991, 189, 1, 37-56, https://doi.org/10.1016/0040-6031(91)87098-H
. [all data]
Takeda, Oguni, et al., 1990
Takeda, K.; Oguni, M.; Suga, H.,
A DTA apparatus for vapour-deposited samples. Characterisation of some vapour-deposited hydrocarbons,
Thermochim. Acta, 1990, 158(1), 195-203. [all data]
Molnar, Rachford, et al., 1984
Molnar, A.; Rachford, R.; Smith, G.V.; Liu, R.,
Heats of hydrogenation by a simple and rapid flow calorimetric method,
Appl. Catal., 1984, 9, 219-223. [all data]
Rogers and Skanupong, 1974
Rogers, D.W.; Skanupong, S.,
Heats of hydrogenation of sixteen terminal monoolefins. The alternating effect,
J. Phys. Chem., 1974, 78, 2569-2572. [all data]
Rogers and McLafferty, 1971
Rogers, D.W.; McLafferty, F.J.,
A new hydrogen calorimeter. Heats of hydrogenation of allyl and vinyl unsaturation adjacent to a ring,
Tetrahedron, 1971, 27, 3765-3775. [all data]
Egger and Benson, 1966
Egger, K.W.; Benson, S.W.,
Nitric oxide and iodine catalyzed isomerization of olefins. VI. Thermodynamic data from equilibrium studies of the geometrical and positional isomerization of n-pentenes,
J. Am. Chem. Soc., 1966, 88, 236-240. [all data]
Karaseva and Andreevskii, 1969
Karaseva, S.Ya.; Andreevskii, D.N.,
Equilibrium in the isomerisation of secondary monochloropentanes and the dehydrochlorination of 2-chloropentane,
Russ. J. Phys. Chem. (Engl. Transl.), 1969, 43, 1236-1238. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Ttrs Temperature of phase transition Vc Critical volume d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrH° Enthalpy of reaction at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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