Propane
- Formula: C3H8
- Molecular weight: 44.0956
- IUPAC Standard InChIKey: ATUOYWHBWRKTHZ-UHFFFAOYSA-N
- CAS Registry Number: 74-98-6
- 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. - Isotopologues:
- Other names: n-Propane; Dimethylmethane; Freon 290; Liquefied petroleum gas; LPG; Propyl hydride; R 290; C3H8; UN 1978; A-108; Hydrocarbon propellant A-108; HC 290
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Data at other public NIST sites:
- Options:
Data at NIST subscription sites:
- NIST / TRC Web Thermo Tables, "lite" edition (thermophysical and thermochemical data)
- NIST / TRC Web Thermo Tables, professional edition (thermophysical and thermochemical data)
NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.
Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Ion clustering 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 |
---|---|---|---|---|---|
ΔfH°gas | -25.02 ± 0.12 | kcal/mol | Ccb | Pittam and Pilcher, 1972 | ALS |
ΔfH°gas | -24.82 ± 0.14 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Hf derived from Heat of Hydrogenation; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -530.39 ± 0.11 | kcal/mol | Ccb | Pittam and Pilcher, 1972 | Corresponding ΔfHºgas = -25.02 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -526.78 ± 0.13 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Hf derived from Heat of Hydrogenation; Corresponding ΔfHºgas = -28.63 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -530.57 ± 0.12 | kcal/mol | Ccb | Rossini, 1934 | Corresponding ΔfHºgas = -24.84 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -527.4 | kcal/mol | Ccb | Guinchant, 1918 | Corresponding ΔfHºgas = -28.0 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 |
---|---|---|---|
8.141 | 50. | Chao J., 1973 | Recommended values are in good agreement with those calculated by [ Pitzer K.S., 1944].; GT |
9.871 | 100. | ||
11.66 | 150. | ||
13.40 | 200. | ||
16.43 | 273.15 | ||
17.59 | 298.15 | ||
17.67 | 300. | ||
22.47 | 400. | ||
26.910 | 500. | ||
30.760 | 600. | ||
34.099 | 700. | ||
36.991 | 800. | ||
39.520 | 900. | ||
41.730 | 1000. | ||
43.659 | 1100. | ||
45.349 | 1200. | ||
46.809 | 1300. | ||
48.090 | 1400. | ||
49.209 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
11.69 | 148.2 | Ernst G., 1970 | Please also see Kistiakowsky G.B., 1940, Kistiakowsky G.B., 1940, 2, Dailey B.P., 1943.; GT |
12.04 | 157.8 | ||
14.00 | 213.1 | ||
14.17 | 219.2 | ||
15.75 | 258.0 | ||
16.19 | 272.38 | ||
17.37 ± 0.02 | 293.15 | ||
17.58 | 300.37 | ||
18.19 ± 0.02 | 313.15 | ||
19.19 ± 0.02 | 333.15 | ||
19.25 | 334.05 | ||
19.66 | 343.65 | ||
20.17 ± 0.02 | 353.15 | ||
20.36 | 360.05 | ||
20.90 | 368.55 | ||
21.62 | 387.75 | ||
25.069 | 452.55 | ||
27.890 | 521.15 | ||
29.099 | 561.95 | ||
30.750 | 603.25 | ||
33.609 | 693.15 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Ion clustering 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
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -28.64 ± 0.14 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Hf derived from Heat of Hydrogenation; ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 40.87 | cal/mol*K | N/A | Kemp and Egan, 1938 | Debye extrapolation, 0 to 15 K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
23.51 | 230. | Vas'kov, 1982 | T = 90 to 230 K. Cp given as 2.2305 J/g*K.; DH |
28.59 | 300. | Goodwin, 1978 | T = 81 to 289 K. Cp data reported for an extended data set; unsmoothed experimental datum.; DH |
23.49 | 230. | Kemp and Egan, 1938 | T = 15 to 230 K.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Ion clustering 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 |
---|---|---|---|---|---|
Tboil | 231.1 ± 0.2 | K | AVG | N/A | Average of 17 out of 21 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 85.5 | K | N/A | Streng, 1971 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tfus | 85.46 | K | N/A | Klipping and Schmidt, 1965 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tfus | 83.25 | K | N/A | Harteck and Edse, 1938 | Uncertainty assigned by TRC = 0.5 K; TRC |
Tfus | 86.05 | K | N/A | Hicks-Brunn and Bruun, 1936 | Uncertainty assigned by TRC = 0.15 K; TRC |
Tfus | 85.35 | K | N/A | Timmermans, 1921 | Uncertainty assigned by TRC = 0.5 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 85. ± 3. | K | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 1.663×10-9 | atm | N/A | Younglove and Ely, 1987 | Uncertainty assigned by TRC = 1.×10-12 atm; TRC |
Ptriple | 1.6674×10-9 | atm | N/A | Goodwin and Haynes, 1982 | TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 369.9 ± 0.2 | K | AVG | N/A | Average of 30 out of 37 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 42.0 ± 0.1 | atm | AVG | N/A | Average of 25 out of 32 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.200 | l/mol | N/A | Ambrose and Tsonopoulos, 1995 | |
Vc | 0.2 | l/mol | N/A | Younglove and Ely, 1987 | Uncertainty assigned by TRC = 0.001 l/mol; TRC |
Vc | 0.198 | l/mol | N/A | Barber, Kay, et al., 1982 | Uncertainty assigned by TRC = 0.004 l/mol; TRC |
Vc | 0.202 | l/mol | N/A | Meyer, 1941 | Uncertainty assigned by TRC = 0.003 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 5.1 ± 0.4 | mol/l | AVG | N/A | Average of 14 out of 15 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 3.884 | kcal/mol | N/A | Majer and Svoboda, 1985 |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
4.4871 | 231.04 | N/A | Kemp and Egan, 1938 | DH |
4.551 | 231.1 | N/A | Majer and Svoboda, 1985 | |
4.49 | 293. | A | Stephenson and Malanowski, 1987 | Based on data from 278. to 332. K.; AC |
4.66 | 233. | A | Stephenson and Malanowski, 1987 | Based on data from 165. to 248. K.; AC |
5.28 | 150. | A | Stephenson and Malanowski, 1987 | Based on data from 104. to 165. K.; AC |
4.54 | 266. | A | Stephenson and Malanowski, 1987 | Based on data from 231. to 281. K.; AC |
4.59 | 344. | A | Stephenson and Malanowski, 1987 | Based on data from 329. to 369. K.; AC |
4.52 | 327. | N/A | Majer, Sváb, et al., 1980 | Based on data from 312. to 367. K.; AC |
4.486 | 256. | N/A | Reid, 1972 | AC |
4.78 | 216. | N/A | Reidel, 1938 | Based on data from 166. to 231. K.; AC |
Enthalpy of vaporization
ΔvapH = A exp(-αTr)
(1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kcal/mol)
Tr = reduced temperature (T / Tc)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 278. to 361. |
---|---|
A (kcal/mol) | 6.67 |
α | 0.0208 |
β | 0.3766 |
Tc (K) | 369.8 |
Reference | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
19.42 | 231.04 | Kemp and Egan, 1938 | DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (atm)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
277.6 to 360.8 | 4.53107 | 1149.36 | 24.906 | Helgeson and Sage, 1967 | Coefficents calculated by NIST from author's data. |
230.6 to 320.7 | 3.97721 | 819.296 | -24.417 | Rips, 1963 | Coefficents calculated by NIST from author's data. |
166.02 to 231.41 | 4.00587 | 834.26 | -22.763 | Kemp and Egan, 1938 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
6.81 | 86. | B | Bondi, 1963 | AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
0.839 | 85.5 | AC | Perkins, Ochoa, et al., 2009 | AC |
0.841 | 85.5 | N/A | Acree, 1991 | AC |
Temperature of phase transition
Ttrs (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|
45.5 | crystaline | glass | Takeda, Oguni, et al., 1990 | DH |
Enthalpy of phase transition
ΔHtrs (kcal/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.8423 | 85.45 | crystaline, I | liquid | Kemp and Egan, 1938 | DH |
Entropy of phase transition
ΔStrs (cal/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
9.857 | 85.45 | crystaline, I | liquid | Kemp and Egan, 1938 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Ion clustering 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:
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
MS - José 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
C3H7- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 419.4 ± 2.0 | kcal/mol | Bran | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrH° | 419.5 ± 4.8 | kcal/mol | Bran | Peerboom, Rademaker, et al., 1992 | gas phase; B |
ΔrH° | 419.0 ± 2.0 | kcal/mol | Bran | DePuy, Bierbaum, et al., 1984 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 411.4 ± 2.1 | kcal/mol | H-TS | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrG° | 411.5 ± 4.9 | kcal/mol | H-TS | Peerboom, Rademaker, et al., 1992 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -29.5 ± 1.2 | kcal/mol | Chyd | Kistiakowsky and Nickle, 1951 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -29.85 ± 0.50 kcal/mol; ALS |
ΔrH° | -29.87 ± 0.10 | kcal/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1935 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -30.115 ± 0.013 kcal/mol; At 355 °K; ALS |
By formula: H2 + C3H7F = C3H8 + HF
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -20.20 ± 0.30 | kcal/mol | Chyd | Lacher, Kianpour, et al., 1956 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -21.11 ± 0.69 kcal/mol; %hf298_gas[kcal/mol]=-66.97±0.71; Kolesov and Kozina, 1986; ALS |
By formula: H2 + C3H7F = C3H8 + HF
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -22.00 ± 0.50 | kcal/mol | Chyd | Lacher, Kianpour, et al., 1956 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -22.9 ± 1.6 kcal/mol; %hf298_gas[kcal/mol]=-66.71±0.62; Kolesov and Kozina, 1986; ALS |
By formula: 2H2 + C3H6Cl2 = C3H8 + 2HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -30.24 ± 0.26 | kcal/mol | Chyd | Lacher, Amador, et al., 1967 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -31.21 ± 0.13 kcal/mol; At 250 C; ALS |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -69.22 ± 0.15 | kcal/mol | Chyd | Conn, Kistiakowsky, et al., 1939 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -69.03 ± 0.14 kcal/mol; At 355 K; ALS |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -70.54 ± 0.25 | kcal/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1936 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -71.28 ± 0.20 kcal/mol; At 355 °K; ALS |
By formula: H2 + C3H7Br = HBr + C3H8
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -10.85 ± 0.22 | kcal/mol | Chyd | Davies, Lacher, et al., 1965 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -10.77 kcal/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 415.6 ± 2.0 | kcal/mol | Bran | DePuy, Gronert, et al., 1989 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 407.2 ± 2.1 | kcal/mol | H-TS | DePuy, Gronert, et al., 1989 | gas phase; B |
By formula: C3H7+ + C3H8 = (C3H7+ • C3H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13.6 | kcal/mol | PHPMS | Sunner, Hirao, et al., 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 29.4 | cal/mol*K | PHPMS | Sunner, Hirao, et al., 1989 | gas phase; M |
By formula: C4H9+ + C3H8 = (C4H9+ • C3H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.6 | kcal/mol | PHPMS | Sunner, Hirao, et al., 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22.3 | cal/mol*K | PHPMS | Sunner, Hirao, et al., 1989 | gas phase; M |
By formula: Fe+ + C3H8 = (Fe+ • C3H8)
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
17.9 (+1.0,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M |
By formula: Co+ + C3H8 = (Co+ • C3H8)
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
30.8 (+1.4,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M |
C3H7BrMg (solution) + (g) = (solution) + Br2Mg (solution)
By formula: C3H7BrMg (solution) + HBr (g) = C3H8 (solution) + Br2Mg (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -73.11 ± 0.53 | kcal/mol | RSC | Holm, 1981 | solvent: Diethyl ether; MS |
By formula: C5O5W (g) + C3H8 (g) = C8H8O5W (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -8.1 ± 2.0 | kcal/mol | EqG | Brown, Ishikawa, et al., 1990 | Temperature range: ca. 300-350 K; MS |
By formula: H2 + C3H7Cl = C3H8 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -15.73 ± 0.16 | kcal/mol | Chyd | Davies, Lacher, et al., 1965 | gas phase; ALS |
By formula: H2 + C3H7Cl = C3H8 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -13.94 ± 0.17 | kcal/mol | Chyd | Davies, Lacher, et al., 1965 | gas phase; ALS |
By formula: C3H7Br + H2 = HBr + C3H8
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -13.57 | kcal/mol | Chyd | Davies, Lacher, et al., 1965 | gas phase; ALS |
Ion clustering data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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: Michael M. Meot-Ner (Mautner) and Sharon G. Lias
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. Searches may be limited to ion clustering reactions. A general reaction search form is also available.
Clustering reactions
By formula: C3H7+ + C3H8 = (C3H7+ • C3H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13.6 | kcal/mol | PHPMS | Sunner, Hirao, et al., 1989 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 29.4 | cal/mol*K | PHPMS | Sunner, Hirao, et al., 1989 | gas phase |
By formula: C4H9+ + C3H8 = (C4H9+ • C3H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.6 | kcal/mol | PHPMS | Sunner, Hirao, et al., 1989 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22.3 | cal/mol*K | PHPMS | Sunner, Hirao, et al., 1989 | gas phase |
By formula: Co+ + C3H8 = (Co+ • C3H8)
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
30.8 (+1.4,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID |
By formula: Fe+ + C3H8 = (Fe+ • C3H8)
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
17.9 (+1.0,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Ion clustering data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Pittam and Pilcher, 1972
Pittam, D.A.; Pilcher, G.,
Measurements of heats of combustion by flame calorimetry. Part 8.-Methane, ethane, propane, n-butane and 2-methylpropane,
J. Chem. Soc. Faraday Trans. 1, 1972, 68, 2224-2229. [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]
Guinchant, 1918
Guinchant, M.J.,
Etude sur la fonction acide dans les derives metheniques et methiniques,
Ann. Chem., 1918, 10, 30-84. [all data]
Chao J., 1973
Chao J.,
Ideal gas thermodynamic properties of ethane and propane,
J. Phys. Chem. Ref. Data, 1973, 2, 427-438. [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]
Ernst G., 1970
Ernst G.,
Ideal and real gas state heat capacities Cp of C3H8, i-C4H10, C2F5Cl, CH2ClCF3, CF2ClCFCl2, and CHF2Cl,
J. Chem. Thermodyn., 1970, 2, 787-791. [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]
Dailey B.P., 1943
Dailey B.P.,
The heat capacities at higher temperatures of ethane and propane,
J. Am. Chem. Soc., 1943, 65, 42-44. [all data]
Kemp and Egan, 1938
Kemp, J.D.; Egan, C.J.,
Hindered rotation of the methyl groups in propane. The heat capacity, vapor pressure, heats of fusion and vaporization of propane. Entropy and density of the gas,
J. Am. Chem. Soc., 1938, 60, 1521-1525. [all data]
Vas'kov, 1982
Vas'kov, E.T.,
Heat capacity of propane,
Deposited Doc., 1982, VINITI 1728-82, 1-15. [all data]
Goodwin, 1978
Goodwin, R.D.,
Specific heats of saturated and compressed liquid propane,
J. Res., 1978, NBS 83, 449-458. [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]
Klipping and Schmidt, 1965
Klipping, G.; Schmidt, F.,
Temperature Measurement with the Vapor Pressure Thermometer,
Kaeltetechnik, 1965, 17, 382-4. [all data]
Harteck and Edse, 1938
Harteck, P.; Edse, R.,
Vapor-pressure Measurement of Propane,
Z. Phys. Chem., Abt. A, 1938, 182, 220. [all data]
Hicks-Brunn and Bruun, 1936
Hicks-Brunn, M.M.; Bruun, J.H.,
The Freezing and Boiling Point of Propane,
J. Am. Chem. Soc., 1936, 58, 810-2. [all data]
Timmermans, 1921
Timmermans, J.,
The Freezing Points of Organic Substances IV. New Exp. Determinations,
Bull. Soc. Chim. Belg., 1921, 30, 62. [all data]
Younglove and Ely, 1987
Younglove, B.A.; Ely, J.F.,
Thermophysical Properties of Fluids II. Methane, Ethane, Propane, Isobutane, and Normal Butane,
J. Phys. Chem. Ref. Data, 1987, 16, 577. [all data]
Goodwin and Haynes, 1982
Goodwin, R.D.; Haynes, W.M.,
Thermophysical Properties of Propane from 85 to 700 K at Pressures to 70 MPa, NBS Monogr. (U. S.) No. 170, 249 pp., 1982. [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]
Barber, Kay, et al., 1982
Barber, J.R.; Kay, W.B.; Teja, A.S.,
A study of the volumetric and phase behavior of binary systems: part I. critical properties of propane + perfluorocyclobutane mixtures.,
AIChE J., 1982, 28, 134-8. [all data]
Meyer, 1941
Meyer, R.E.,
, Ph.D. Thesis, Penn. State Univ., Univ. Park, PA, 1941. [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]
Majer, Sváb, et al., 1980
Majer, V.; Sváb, L.; Svoboda, V.,
Enthalpies of vaporization and cohesive energies for a group of chlorinated hydrocarbons,
The Journal of Chemical Thermodynamics, 1980, 12, 9, 843-847, https://doi.org/10.1016/0021-9614(80)90028-2
. [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]
Reidel, 1938
Reidel, L.,
Z. Ges. Kalte-Ind., 1938, 45, 221. [all data]
Helgeson and Sage, 1967
Helgeson, N.L.; Sage, B.H.,
Latent Heat of Vaporization of Propane,
J. Chem. Eng. Data, 1967, 12, 1, 47-49, https://doi.org/10.1021/je60032a015
. [all data]
Rips, 1963
Rips, S.M.,
On a Feasible Level of Filling in of Reservoires by Liquid Hydrocarbons,
Khim. Prom. (Moscow), 1963, 8, 610-613. [all data]
Bondi, 1963
Bondi, A.,
Heat of Siblimation of Molecular Crystals: A Catalog of Molecular Structure Increments.,
J. Chem. Eng. Data, 1963, 8, 3, 371-381, https://doi.org/10.1021/je60018a027
. [all data]
Perkins, Ochoa, et al., 2009
Perkins, Richard A.; Ochoa, Jesus C. Sanchez; Magee, Joseph W.,
Thermodynamic Properties of Propane. II. Molar Heat Capacity at Constant Volume from (85 to 345) K with Pressures to 35 MPa,
J. Chem. Eng. Data, 2009, 54, 12, 3192-3201, https://doi.org/10.1021/je900137r
. [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]
DePuy, Gronert, et al., 1989
DePuy, C.H.; Gronert, S.; Barlow, S.E.; Bierbaum, V.M.; Damrauer, R.,
The Gas Phase Acidities of the Alkanes,
J. Am. Chem. Soc., 1989, 111, 6, 1968, https://doi.org/10.1021/ja00188a003
. [all data]
Peerboom, Rademaker, et al., 1992
Peerboom, R.A.L.; Rademaker, G.J.; Dekoning, L.J.; Nibbering, N.M.M.,
Stabilization of Cycloalkyl Carbanions in the Gas Phase,
Rapid Commun. Mass Spectrom., 1992, 6, 6, 394, https://doi.org/10.1002/rcm.1290060608
. [all data]
DePuy, Bierbaum, et al., 1984
DePuy, C.H.; Bierbaum, V.M.; Damrauer, R.,
Relative Gas-Phase Acidities of the Alkanes,
J. Am. Chem. Soc., 1984, 106, 4051. [all data]
Kistiakowsky and Nickle, 1951
Kistiakowsky, G.B.; Nickle, A.G.,
Ethane-ethylene and propane-propylene equilibria,
Faraday Discuss. Chem. Soc., 1951, 10, 175-187. [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]
Kistiakowsky, Ruhoff, et al., 1935
Kistiakowsky, G.B.; Ruhoff, J.R.; Smith, H.A.; Vaughan, W.E.,
Heats of organic reactions. II. Hydrogenation of some simpler olefinic hydrocarbons,
J. Am. Chem. Soc., 1935, 57, 876-882. [all data]
Lacher, Kianpour, et al., 1956
Lacher, J.R.; Kianpour, A.; Park, J.D.,
Reaction heats of organic halogen compounds. VI. The catalytic hydrogenation of some alkyl fluorides,
J. Phys. Chem., 1956, 60, 1454-1455. [all data]
Kolesov and Kozina, 1986
Kolesov, V.P.; Kozina, M.P.,
Thermochemistry of organic and organohalogen compounds,
Russ. Chem. Rev., 1986, 55, 912. [all data]
Lacher, Amador, et al., 1967
Lacher, J.R.; Amador, A.; Park, J.D.,
Reaction heats of organic compounds. Part 5.-Heats of hydrogenation of dichloromethane, 1,1- and 1,2-dichloroethane and 1,2-dichloropropane,
Trans. Faraday Soc., 1967, 63, 1608-1611. [all data]
Conn, Kistiakowsky, et al., 1939
Conn, J.B.; Kistiakowsky, G.B.; Smith, E.A.,
Heats of organic reactions. VIII. Some further hydrogenations, including those of some acetylenes,
J. Am. Chem. Soc., 1939, 61, 1868-1876. [all data]
Kistiakowsky, Ruhoff, et al., 1936
Kistiakowsky, G.B.; Ruhoff, J.R.; Smith, H.A.; Vaughan, W.E.,
Heats of organic reactions. IV. Hydrogenation of some dienes and of benzene,
J. Am. Chem. Soc., 1936, 58, 146-153. [all data]
Davies, Lacher, et al., 1965
Davies, J.; Lacher, J.R.; Park, J.D.,
Reaction heats of organic compounds. Part 4.-Heats of hydrogenation of n- and iso-Propyl bromides and chlorides,
Trans. Faraday Soc., 1965, 61, 2413-2416. [all data]
Sunner, Hirao, et al., 1989
Sunner, J.A.; Hirao, K.; Kebarle, P.,
Hydride - Transfer Reactions. Temperature Dependence of Rate Constants for i-C3H7+ + HC(CH3)3 = C3H8 + C(CH3)3+. Clusters of i-C3H7+ and t-C4H9+ with Propane and Isobutane,
J. Phys. Chem., 1989, 93, 10, 4010, https://doi.org/10.1021/j100347a030
. [all data]
Armentrout and Kickel, 1994
Armentrout, P.B.; Kickel, B.L.,
Gas Phase Thermochemistry of Transition Metal Ligand Systems: Reassessment of Values and Periodic Trends, in Organometallic Ion Chemistry, B. S. Freiser, ed, 1994. [all data]
Holm, 1981
Holm, T.,
J. Chem. Soc., Perkin Trans. II, 1981, 464.. [all data]
Brown, Ishikawa, et al., 1990
Brown, C.E.; Ishikawa, Y.; Hackett, P.A.; Rayner, D.M.,
J. Am. Chem. Soc., 1990, 112, 2530. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Ion clustering 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 Ptriple Triple point pressure S°liquid Entropy of liquid at standard conditions T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Ttrs Temperature of phase transition Vc Critical volume ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition ΔcH°gas Enthalpy of combustion of gas 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions ΔsubH Enthalpy of sublimation ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
- The National Institute of Standards and Technology (NIST) uses its best efforts to deliver a high quality copy of the Database and to verify that the data contained therein have been selected on the basis of sound scientific judgment. However, NIST makes no warranties to that effect, and NIST shall not be liable for any damage that may result from errors or omissions in the Database.
- Customer support for NIST Standard Reference Data products.