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
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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, IR Spectrum, Mass spectrum (electron ionization), Vibrational and/or electronic energy levels, 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
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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:
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
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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 |
---|---|---|---|---|---|
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)
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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)
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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
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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:
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 |
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 |
---|---|---|---|---|
0.0015 | 2700. | L | N/A | |
0.0014 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.0014 | L | N/A | ||
0.0015 | 2700. | L | N/A | |
0.0014 | V | N/A |
IR Spectrum
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Data compiled by: Coblentz Society, Inc.
Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director
Mass spectrum (electron ionization)
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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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
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Due to licensing restrictions, this spectrum cannot be downloaded.
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. |
---|---|
NIST MS number | 18863 |
Vibrational and/or electronic energy levels
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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: Takehiko Shimanouchi
Symmetry: C2ν Symmetry Number σ = 2
Sym. | No | Approximate | Selected Freq. | Infrared | Raman | Comments | ||||
---|---|---|---|---|---|---|---|---|---|---|
Species | type of mode | Value | Rating | Value | Phase | Value | Phase | |||
a1 | 1 | CH3 d-str | 2977 | C | 2977 | gas | ||||
a1 | 2 | CH3 s-str | 2962 | D | 2962 | gas | ||||
a1 | 3 | CH2 s-str | 2887 | C | 2887 | gas | ||||
a1 | 4 | CH3 d-deform | 1476 | C | 1476 | gas | ||||
a1 | 5 | CH2 scis | 1462 | C | 1462 | gas | ||||
a1 | 6 | CH3 s-deform | 1392 | C | 1392 | gas | ||||
a1 | 7 | CH3 rock | 1158 | C | 1158 | gas | 1152 W | liq. | ||
a1 | 8 | CC str | 869 | C | 869 | gas | 867 S | liq. | ||
a1 | 9 | CCC deform | 369 | C | 369 | gas | 375 W | liq. | ||
a2 | 10 | CH3 d-str | 2967 | C | ia | 2967 M | liq. | |||
a2 | 11 | CH3 d-deform | 1451 | C | ia | 1451 S | liq. | |||
a2 | 12 | CH2 twist | 1278 | C | ia | 1278 W | liq. | |||
a2 | 13 | CH3 rock | 940 | D | ia | 940 VW | liq. | |||
a2 | 14 | Torsion | 216 | C | ia | MW ( ?/?) | ||||
b1 | 15 | CH3 d-str | 2968 | C | 2968 | gas | ||||
b1 | 16 | CH3 s-str | 2887 | C | 2887 | gas | OV(ν3) | |||
b1 | 17 | CH3 d-deform | 1464 | C | 1464 | gas | ||||
b1 | 18 | CH3 s-deform | 1378 | C | 1378 | gas | ||||
b1 | 19 | CH2 wag | 1338 | C | 1338 | gas | 1338 M | liq. | ||
b1 | 20 | CC str | 1054 | C | 1054 | gas | 1054 M | liq. | ||
b1 | 21 | CH3 rock | 922 | C | 922 | gas | ||||
b2 | 22 | CH3 d-str | 2973 | C | 2973 | gas | ||||
b2 | 23 | CH2 a-str | 2968 | C | 2968 | gas | ||||
b2 | 24 | CH3 d-deform | 1472 | C | 1472 | gas | ||||
b2 | 25 | CH3 rock | 1192 | C | 1192 | gas | ||||
b2 | 26 | CH2 rock | 748 | C | 748 | gas | ||||
b2 | 27 | Torsion | 268 | C | MW ( ?/?) | |||||
Source: Shimanouchi, 1972
Notes
S | Strong |
M | Medium |
W | Weak |
VW | Very weak |
ia | Inactive |
OV | Overlapped by band indicated in parentheses. |
MW | Torsional Frequency calculated from microwave spectroscopic data. |
C | 3~6 cm-1 uncertainty |
D | 6~15 cm-1 uncertainty |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), Vibrational and/or electronic energy levels, 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,
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), Vibrational and/or electronic energy levels, 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 d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K 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
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