Methane
- Formula: CH4
- Molecular weight: 16.0425
- IUPAC Standard InChIKey: VNWKTOKETHGBQD-UHFFFAOYSA-N
- CAS Registry Number: 74-82-8
- 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: Marsh gas; Methyl hydride; CH4; Fire Damp; R 50; Biogas; R 50 (refrigerant)
- 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, 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 as indicated in comments:
DRB - Donald R. Burgess, Jr.
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 | -17.89 | kcal/mol | Review | Chase, 1998 | Data last reviewed in March, 1961 |
ΔfH°gas | -17.8 ± 0.07 | kcal/mol | Review | Manion, 2002 | adopted recommendation of Gurvich, Veyts, et al., 1991; DRB |
ΔfH°gas | -17.8 ± 0.1 | kcal/mol | Ccb | Pittam and Pilcher, 1972 | ALS |
ΔfH°gas | -17.889 ± 0.075 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Hf derived from Heat of Hydrogenation; ALS |
ΔfH°gas | -17.54 ± 0.26 | kcal/mol | Ccb | Roth and Banse, 1932 | Reanalyzed by Cox and Pilcher, 1970, Original value = -17.97 kcal/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -212.88 ± 0.09 | kcal/mol | Ccb | Pittam and Pilcher, 1972 | Corresponding ΔfHºgas = -17.80 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -212.798 ± 0.072 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Hf derived from Heat of Hydrogenation; Corresponding ΔfHºgas = -17.883 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -213.14 ± 0.26 | kcal/mol | Ccb | Roth and Banse, 1932 | Reanalyzed by Cox and Pilcher, 1970, Original value = -212.07 ± 0.25 kcal/mol; Corresponding ΔfHºgas = -17.54 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -212.753 ± 0.072 | kcal/mol | Cm | Rossini, 1931 | Corresponding ΔfHºgas = -17.928 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 45.09 ± 0.10 | cal/mol*K | N/A | Colwell J.H., 1963 | The calorimetric value is significantly higher than the statistically calculated entropy, 186.26 J/mol*K, which remains the best value for use in thermodynamic calculations [ Vogt G.J., 1976, Friend D.G., 1989, Gurvich, Veyts, et al., 1989]. Earlier the value of 185.3 J/mol*K was calculated from experimental data [ Giauque W.F., 1931]. The value of S(298.15 K)=185.94 J/mol*K was obtained by high accuracy ab initio calculation [ East A.L.L., 1997].; GT |
Quantity | Value | Units | Method | Reference | Comment |
S°gas,1 bar | 44.515 | cal/mol*K | Review | Chase, 1998 | Data last reviewed in March, 1961 |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
8.346 ± 0.060 | 279. | Halford J.O., 1957 | GT |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
7.954 | 100. | Gurvich, Veyts, et al., 1989 | p=1 bar. Because of more precise method of calculation, the recommended values are more accurate, especially at high temperatures, than those obtained by [ McDowell R.S., 1963] and often regarded as reference data [ Friend D.G., 1989].; GT |
8.009 | 200. | ||
8.530 | 298.15 | ||
8.547 | 300. | ||
9.711 | 400. | ||
11.14 | 500. | ||
12.61 | 600. | ||
14.01 | 700. | ||
15.32 | 800. | ||
16.52 | 900. | ||
17.63 | 1000. | ||
18.62 | 1100. | ||
19.52 | 1200. | ||
20.33 | 1300. | ||
21.06 | 1400. | ||
21.72 | 1500. | ||
22.31 | 1600. | ||
22.84 | 1700. | ||
23.33 | 1800. | ||
23.78 | 1900. | ||
24.197 | 2000. | ||
24.577 | 2100. | ||
24.931 | 2200. | ||
25.263 | 2300. | ||
25.574 | 2400. | ||
25.868 | 2500. | ||
26.145 | 2600. | ||
26.410 | 2700. | ||
26.663 | 2800. | ||
26.905 | 2900. | ||
27.139 | 3000. |
Gas Phase Heat Capacity (Shomate Equation)
Cp° = A + B*t + C*t2 + D*t3 +
E/t2
H° − H°298.15= A*t + B*t2/2 +
C*t3/3 + D*t4/4 − E/t + F − H
S° = A*ln(t) + B*t + C*t2/2 + D*t3/3 −
E/(2*t2) + G
Cp = heat capacity (cal/mol*K)
H° = standard enthalpy (kcal/mol)
S° = standard entropy (cal/mol*K)
t = temperature (K) / 1000.
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 298. to 1300. | 1300. to 6000. |
---|---|---|
A | -0.168028 | 20.50960 |
B | 25.92670 | 2.692321 |
C | -10.16290 | -0.505293 |
D | 1.401240 | 0.033028 |
E | 0.162181 | -6.315060 |
F | -18.36610 | -36.69520 |
G | 37.93411 | 53.63631 |
H | -17.89510 | -17.89510 |
Reference | Chase, 1998 | Chase, 1998 |
Comment | Data last reviewed in March, 1961 | Data last reviewed in March, 1961 |
Phase change data
Go To: Top, Gas phase thermochemistry 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 as indicated in comments:
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 | 111. ± 2. | K | AVG | N/A | Average of 13 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 85.7 | K | N/A | Streng, 1971 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tfus | 90.6 | K | N/A | Van't Zelfde, Omar, et al., 1968 | Uncertainty assigned by TRC = 0.3 K; TRC |
Tfus | 91.2 | K | N/A | Timmermans, 1935 | Uncertainty assigned by TRC = 2. K; TRC |
Tfus | 90.6 | K | N/A | Clusius, 1929 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tfus | 90.5 | K | N/A | Eucken and Karwat, 1924 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 90.67 ± 0.03 | K | AVG | N/A | Average of 25 out of 32 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 0.1154 ± 0.0006 | atm | AVG | N/A | Average of 20 out of 23 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 190.6 ± 0.3 | K | AVG | N/A | Average of 19 out of 23 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 45.5 ± 0.3 | atm | AVG | N/A | Average of 16 out of 21 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.09860 | l/mol | N/A | Ambrose and Tsonopoulos, 1995 | |
Vc | 0.09852 | l/mol | N/A | Younglove and Ely, 1987 | TRC |
Vc | 0.100 | l/mol | N/A | Terry, Lynch, et al., 1969 | Uncertainty assigned by TRC = 0.001 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 10.1 ± 0.2 | mol/l | AVG | N/A | Average of 16 out of 17 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
2.036 | 99.54 | N/A | Vogt and Pitzer, 1976 | P = 2.81 kPa Data from Frank and Clusius, 1937 and 39FRA/CLU.; DH |
2.1 | 101. | N/A | Stock, Henning, et al., 2006 | Based on data from 92. to 110. K. See also Boublik, Fried, et al., 1984.; AC |
2.1 | 105. | A | Stephenson and Malanowski, 1987 | Based on data from 90. to 120. K.; AC |
2.0 | 134. | A | Stephenson and Malanowski, 1987 | Based on data from 115. to 149. K.; AC |
2.1 | 174. | A | Stephenson and Malanowski, 1987 | Based on data from 148. to 189. K.; AC |
1.95 | 111.7 | N/A | Majer and Svoboda, 1985 | |
2.1 | 112. | N/A | Ott, Goates, et al., 1972 | Based on data from 91. to 127. K. See also Boublik, Fried, et al., 1984.; AC |
2.0 | 175. | N/A | Ott, Goates, et al., 1972 | Based on data from 91. to 190. K.; AC |
1.9 | 137. | N/A | Reid, 1972 | AC |
2.1 | 175. | N/A | Ambrose, Counsell, et al., 1970 | Based on data from 100. to 190. K.; AC |
2.0 | 112. | C | Hestermans and White, 1961 | AC |
1.8 | 130. | C | Hestermans and White, 1961 | AC |
1.4 | 160. | C | Hestermans and White, 1961 | AC |
0.96 | 180. | C | Hestermans and White, 1961 | AC |
2.0 | 149. | N/A | Hestermans and White, 1961 | Based on data from 109. to 189. K.; AC |
2.0 ± 0.02 | 99. | N/A | Frank and Clusius, 1939 | 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) | 112. to 180. |
---|---|
A (kcal/mol) | 2.416 |
α | -0.22 |
β | 0.388 |
Tc (K) | 190.6 |
Reference | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
20.45 | 99.54 | Vogt and Pitzer, 1976 | P; 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 |
---|---|---|---|---|---|
90.99 to 189.99 | 3.9838 | 443.028 | -0.49 | Prydz and Goodwin, 1972 | Coefficents calculated by NIST from author's data. |
96.89 to 110.19 | 1.99682 | 125.819 | -48.823 | Regnier, 1972 | Coefficents calculated by NIST from author's data. |
93.04 to 107.84 | 3.79664 | 403.106 | -5.479 | Cutler and Morrison, 1965 | Coefficents calculated by NIST from author's data. |
110.00 to 190.5 | 4.21490 | 516.689 | 11.223 | Hestermans and White, 1961 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
2.3 | 72. | N/A | Stephenson and Malanowski, 1987 | Based on data from 53. to 91. K.; AC |
2.2 | 72. | N/A | Bondi, 1963 | Based on data from 54. to 90. K. See also Armstrong, Brickwedde, et al., 1955.; AC |
2.39 | 84. | N/A | Jones, 1960 | Based on data from 79. to 89. K.; AC |
2.3 | 63. | A,MS | Tickner and Lossing, 1951 | Based on data from 48. to 78. K.; AC |
2.30 | 77. | A | Stull, 1947 | Based on data from 67. to 88. K.; AC |
Enthalpy of phase transition
ΔHtrs (kcal/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.02236 | 20.53 | crystaline, II | crystaline, I | Vogt and Pitzer, 1976 | Lambda transition.; DH |
0.2245 | 90.67 | crystaline, I | liquid | Vogt and Pitzer, 1976 | DH |
Entropy of phase transition
ΔStrs (cal/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
1.089 | 20.53 | crystaline, II | crystaline, I | Vogt and Pitzer, 1976 | Lambda; DH |
2.476 | 90.67 | crystaline, I | liquid | Vogt and Pitzer, 1976 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change 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
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
MS - José A. Martinho Simões
ALS - 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.
Reactions 1 to 50
CH3- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 416.74 ± 0.70 | kcal/mol | D-EA | Ellison, Engelking, et al., 1978 | gas phase; B |
ΔrH° | 418.0 ± 3.5 | kcal/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
ΔrH° | >404.18 ± 0.10 | kcal/mol | G+TS | Bohme, Lee-Ruff, et al., 1972 | gas phase; B |
ΔrH° | 414.80 | kcal/mol | N/A | Check, Faust, et al., 2001 | gas phase; FeBr3; ; ΔS(EA)=9.3; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 408.66 ± 0.80 | kcal/mol | H-TS | Ellison, Engelking, et al., 1978 | gas phase; B |
ΔrG° | 409.9 ± 3.6 | kcal/mol | H-TS | Graul and Squires, 1990 | gas phase; B |
ΔrG° | >396.10 | kcal/mol | IMRB | Bohme, Lee-Ruff, et al., 1972 | gas phase; B |
ΔrG° | 407.30 | kcal/mol | N/A | Check, Faust, et al., 2001 | gas phase; FeBr3; ; ΔS(EA)=9.3; B |
By formula: (CH5+ • CH4) + CH4 = (CH5+ • 2CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.3 ± 0.3 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
ΔrH° | 5.9 | kcal/mol | PHPMS | Hiraoka and Kebarle, 1975 | gas phase; M |
ΔrH° | 1.5 | kcal/mol | HPMS | Field and Beggs, 1971 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.9 | cal/mol*K | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
ΔrS° | 24.4 | cal/mol*K | PHPMS | Hiraoka and Kebarle, 1975 | gas phase; M |
ΔrS° | 7.2 | cal/mol*K | HPMS | Field and Beggs, 1971 | gas phase; Entropy change is questionable; M |
By formula: CH5+ + CH4 = (CH5+ • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.9 ± 0.3 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
ΔrH° | 7.4 | kcal/mol | PHPMS | Hiraoka and Kebarle, 1975 | gas phase; M |
ΔrH° | 4.1 | kcal/mol | HPMS | Field and Beggs, 1971 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22.1 | cal/mol*K | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
ΔrS° | 20.8 | cal/mol*K | PHPMS | Hiraoka and Kebarle, 1975 | gas phase; M |
ΔrS° | 12.4 | cal/mol*K | HPMS | Field and Beggs, 1971 | gas phase; Entropy change is questionable; M |
By formula: C2H5+ + CH4 = (C2H5+ • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.50 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
ΔrH° | 6.6 | kcal/mol | PHPMS | Hiroka and Kebarle, 1975 | gas phase; M |
ΔrH° | 2.4 | kcal/mol | HPMS | Field and Beggs, 1971 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22.2 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
ΔrS° | 23.4 | cal/mol*K | PHPMS | Hiroka and Kebarle, 1975 | gas phase; M |
ΔrS° | 8.6 | cal/mol*K | HPMS | Field and Beggs, 1971 | gas phase; Entropy change is questionable; M |
By formula: (Co+ • 2CH4) + CH4 = (Co+ • 3CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11. | kcal/mol | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20. | cal/mol*K | N/A | Kemper, Bushnell, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
9.8 (+1.2,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
0.7 | 477. | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
By formula: Co+ + CH4 = (Co+ • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 19.8 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(530 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
21.5 (+1.6,-0.) | CID | Haynes and Armentrout, 1996 | gas phase; guided ion beam CID; M | |
21.5 (+1.4,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M | |
22.5 (+0.5,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(530 K); M |
By formula: (Co+ • CH4) + H2 = (Co+ • H2 • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 22.9 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2H2, ΔrS(440 K); Kemper, Bushnell, et al., 1993, 2; M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
17.4 (+0.8,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2H2, ΔrS(440 K); Kemper, Bushnell, et al., 1993, 2; M |
By formula: (Co+ • H2) + CH4 = (Co+ • CH4 • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 21.8 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+)2H2, ΔrS(440 K); Kemper, Bushnell, et al., 1993, 2; M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
22.6 (+1.2,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+)2H2, ΔrS(440 K); Kemper, Bushnell, et al., 1993, 2; M |
(g) = C5MnO5 (g) + (g)
By formula: C6H3MnO5 (g) = C5MnO5 (g) + CH4 (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.9 ± 3.6 | kcal/mol | PIMS | Martinho Simões and Beauchamp, 1990 | The reaction enthalpy was derived from the appearance energy of Mn(CO)5(+), 224.8 ± 1.1 kcal/mol, using Mn(CO)5(Me) as the neutral precursor, together with the adiabatic ionization energy of Mn(CO)5 radical, 179. ± 3.3 kcal/mol Martinho Simões and Beauchamp, 1990; MS |
By formula: (Co+ • CH4) + CH4 = (Co+ • 2CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 26.1 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(500 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
22.9 (+1.2,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M | |
24.8 (+1.0,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(500 K); M |
By formula: (CH5+ • 2CH4) + CH4 = (CH5+ • 3CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.1 ± 0.2 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
ΔrH° | 4.1 | kcal/mol | PHPMS | Hiraoka and Kebarle, 1975 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22.4 | cal/mol*K | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
ΔrS° | 26.1 | cal/mol*K | PHPMS | Hiraoka and Kebarle, 1975 | gas phase; M |
By formula: (CH5+ • 3CH4) + CH4 = (CH5+ • 4CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.0 ± 0.2 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
ΔrH° | 3.9 | kcal/mol | PHPMS | Hiraoka and Kebarle, 1975 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 23.7 | cal/mol*K | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
ΔrS° | 26.6 | cal/mol*K | PHPMS | Hiraoka and Kebarle, 1975 | gas phase; M |
(g) + CH3BrMg (solution) = (solution) + Br2Mg (solution)
By formula: HBr (g) + CH3BrMg (solution) = CH4 (solution) + Br2Mg (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -65.61 ± 0.53 | kcal/mol | RSC | Holm, 1981 | solvent: Diethyl ether; The enthalpy of formation was calculated using the assumptions and the auxiliary data in Holm, 1981, except for the organic compound, whose enthalpy of formation was quoted from Pedley, 1994; MS |
By formula: (Co+ • CH4) + C2H6 = (Co+ • C2H6 • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 25.9 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2CH4, ΔrS(480 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
28.4 (+1.3,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2CH4, ΔrS(480 K); M |
C63H91CoN13O14P (solution) = (solution) + (solution)
By formula: C63H91CoN13O14P (solution) = C63H88CoN14O14P (solution) + CH4 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 37.0 ± 3.1 | kcal/mol | KinS | Martin and Finke, 1990 | solvent: Ethylene glycol; Please also see Martin and Finke, 1992. The reaction enthalpy relies on 41.0 ± 3.0 kcal/mol for the reaction activation enthalpy. The reaction refers to "base-on" cobalamine.; MS |
By formula: C3H7+ + CH4 = (C3H7+ • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.59 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
ΔrH° | 3.4 | kcal/mol | PHPMS | Hiraoka and Kebarle, 1976 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 17.4 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
ΔrS° | 20. | cal/mol*K | PHPMS | Hiraoka and Kebarle, 1976 | gas phase; M |
By formula: HI + CH3I = CH4 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -12.56 ± 0.13 | kcal/mol | Eqk | Golden, Walsh, et al., 1965 | gas phase; ALS |
ΔrH° | -12.67 ± 0.05 | kcal/mol | Eqk | Goy and Pritchard, 1965 | gas phase; ALS |
ΔrH° | -11.0 ± 1.3 | kcal/mol | Cm | Nichol and Ubbelohde, 1952 | gas phase; ALS |
By formula: (C2H5+ • 9CH4) + CH4 = (C2H5+ • 10CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.91 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22. | cal/mol*K | N/A | Hiraoka, Mori, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
By formula: (C3H7+ • 7CH4) + CH4 = (C3H7+ • 8CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.98 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22. | cal/mol*K | N/A | Hiraoka, Mori, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
By formula: (C4H9+ • 8CH4) + CH4 = (C4H9+ • 9CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.86 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20. | cal/mol*K | N/A | Hiraoka, Mori, et al., 1993 | gas phase; Entropy change calculated or estimated; M |
By formula: (CH5+ • 8CH4) + CH4 = (CH5+ • 9CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.54 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20. | cal/mol*K | N/A | Hiraoka and Mori, 1989 | gas phase; Entropy change calculated or estimated; M |
By formula: (Co+ • H2O) + CH4 = (Co+ • CH4 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 27.0 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(525 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
25.9 (+0.7,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(525 K); M |
By formula: (H3O+ • CH4) + CH4 = (H3O+ • 2CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.4 | kcal/mol | HPMS | Bennet and Field, 1972 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 8.1 | cal/mol*K | HPMS | Bennet and Field, 1972 | gas phase; Entropy change is questionable; M |
By formula: (Co+ • C2H6) + CH4 = (Co+ • CH4 • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 26.4 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(490 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
24.4 (+1.1,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(490 K); M |
By formula: H4N+ + CH4 = (H4N+ • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.6 | kcal/mol | HPMS | Bennet and Field, 1972, 2 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 15.5 | cal/mol*K | HPMS | Bennet and Field, 1972, 2 | gas phase; Entropy change is questionable; M |
By formula: HBr (g) + CH3Li (cr) = CH4 (g) + BrLi (cr)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -75.84 ± 0.48 | kcal/mol | RSC | Holm, 1974 | Please also see Pedley and Rylance, 1977. The reaction enthalpy was quoted from Pedley and Rylance, 1977. See Liebman, Martinho Simões, et al., 1995 for comments; MS |
By formula: 2H2 + CH2Cl2 = CH4 + 2HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -39.05 ± 0.30 | kcal/mol | Chyd | Lacher, Amador, et al., 1967 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -40.07 ± 0.30 kcal/mol; At 250 C; ALS |
(l) + ( • 100) (solution) = 2 (g) + ( • 100) (solution)
By formula: C2H6Zn (l) + (H2O4S • 100H2O) (solution) = 2CH4 (g) + (O4SZn • 100H2O) (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -81.7 ± 0.2 | kcal/mol | RSC | Carson, Hartley, et al., 1949 | Please also see Pedley and Rylance, 1977 and Cox and Pilcher, 1970, 2.; MS |
By formula: (CH5+ • 4CH4) + CH4 = (CH5+ • 5CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.8 ± 0.2 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.8 | cal/mol*K | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
By formula: (CH5+ • 5CH4) + CH4 = (CH5+ • 6CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.7 ± 0.2 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25.3 | cal/mol*K | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
By formula: (CH5+ • 6CH4) + CH4 = (CH5+ • 7CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.7 ± 0.2 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 26.5 | cal/mol*K | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
By formula: (CH5+ • 7CH4) + CH4 = (CH5+ • 8CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.0 ± 0.2 | kcal/mol | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21.6 | cal/mol*K | PHPMS | Hiraoka and Mori, 1989 | gas phase; M |
By formula: (C2H5+ • 2CH4) + CH4 = (C2H5+ • 3CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.28 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 17.9 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C2H5+ • 3CH4) + CH4 = (C2H5+ • 4CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.26 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 18.4 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C2H5+ • 4CH4) + CH4 = (C2H5+ • 5CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.22 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 18.9 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C2H5+ • 5CH4) + CH4 = (C2H5+ • 6CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.21 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 19.4 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C2H5+ • 6CH4) + CH4 = (C2H5+ • 7CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.13 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20.7 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C2H5+ • 7CH4) + CH4 = (C2H5+ • 8CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.10 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21.0 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C2H5+ • 8CH4) + CH4 = (C2H5+ • 9CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.08 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21.8 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C3H7+ • 2CH4) + CH4 = (C3H7+ • 3CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.26 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 18.4 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C3H7+ • 3CH4) + CH4 = (C3H7+ • 4CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.20 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 19.0 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C3H7+ • 4CH4) + CH4 = (C3H7+ • 5CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.20 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20.9 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C3H7+ • 5CH4) + CH4 = (C3H7+ • 6CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.19 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21.0 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C3H7+ • 6CH4) + CH4 = (C3H7+ • 7CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.16 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21.8 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C4H9+ • 2CH4) + CH4 = (C4H9+ • 3CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.37 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 19.7 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C4H9+ • 3CH4) + CH4 = (C4H9+ • 4CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.36 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20.0 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C4H9+ • 4CH4) + CH4 = (C4H9+ • 5CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.21 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 19.4 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C4H9+ • 5CH4) + CH4 = (C4H9+ • 6CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.09 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 19.3 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C4H9+ • 6CH4) + CH4 = (C4H9+ • 7CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.05 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 19.7 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
By formula: (C4H9+ • 7CH4) + CH4 = (C4H9+ • 8CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.99 | kcal/mol | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20.1 | cal/mol*K | PHPMS | Hiraoka, Mori, et al., 1993 | gas phase; M |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Chase, 1998
Chase, M.W., Jr.,
NIST-JANAF Themochemical Tables, Fourth Edition,
J. Phys. Chem. Ref. Data, Monograph 9, 1998, 1-1951. [all data]
Manion, 2002
Manion, J.A.,
Evaluated Enthalpies of Formation of the Stable Closed Shell C1 and C2 Chlorinated Hydrocarbons,
J. Phys. Chem. Ref. Data, 2002, 31, 1, 123-172, https://doi.org/10.1063/1.1420703
. [all data]
Gurvich, Veyts, et al., 1991
Thermodynamic Properties of Individual Substances, 4th edition, Volume 2, Gurvich, L.V.; Veyts, I.V.; Alcock, C.B.;, ed(s)., Hemisphere, New York, 1991. [all data]
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]
Roth and Banse, 1932
Roth, W.A.; Banse, H.,
Die verbrennungs- und bildungswarme von kohlenoxyd und methan,
Arch. Eisenhutten., 1932, 6, 43-46. [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]
Rossini, 1931
Rossini, F.D.,
The heats of combustion of methane and carbon monoxide,
J. Res. NBS, 1931, 6, 37-49. [all data]
Colwell J.H., 1963
Colwell J.H.,
Thermodynamic properties of CH4 and CD4. Interpretation of the properties of solid,
J. Chem. Phys., 1963, 39, 635-653. [all data]
Vogt G.J., 1976
Vogt G.J.,
Entropy and heat capacity of methane; spin-species conversion,
J. Chem. Thermodyn., 1976, 8, 1011-1031. [all data]
Friend D.G., 1989
Friend D.G.,
Thermophysical properties of methane,
J. Phys. Chem. Ref. Data, 1989, 18, 583-638. [all data]
Gurvich, Veyts, et al., 1989
Gurvich, L.V.; Veyts, I.V.; Alcock, C.B.,
Thermodynamic Properties of Individual Substances, 4th ed.; Vols. 1 and 2, Hemisphere, New York, 1989. [all data]
Giauque W.F., 1931
Giauque W.F.,
The entropies of methane and ammonia,
Phys. Rev., 1931, 38, 196-197. [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]
Halford J.O., 1957
Halford J.O.,
Standard heat capacities of gaseous methanol, ethanol, methane and ethane at 279 K by thermal conductivity,
J. Phys. Chem., 1957, 61, 1536-1539. [all data]
McDowell R.S., 1963
McDowell R.S.,
Thermodynamic functions of methane,
J. Chem. Eng. Data, 1963, 8, 547-548. [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]
Van't Zelfde, Omar, et al., 1968
Van't Zelfde, P.; Omar, M.H.; LePair-Schroten, H.G.M.; Dokoupil, Z.,
Solid-liquid equilibrium diagram for the argon + methane system.,
Physica (Amsterdam), 1968, 38, 241-51. [all data]
Timmermans, 1935
Timmermans, J.,
Researches in Stoichiometry. I. The Heat of Fusion of Organic Compounds.,
Bull. Soc. Chim. Belg., 1935, 44, 17-40. [all data]
Clusius, 1929
Clusius, K.,
The specific heat of several condensed gases between 10deg. abs. and their triple point.,
Z. Phys. Chem., Abt. B, 1929, 3, 41. [all data]
Eucken and Karwat, 1924
Eucken, A.; Karwat, E.,
Determination of the heat content of several condensed gases,
Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1924, 112, 467. [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]
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]
Terry, Lynch, et al., 1969
Terry, M.J.; Lynch, J.T.; Bunclark, M.; Mansell, K.R.; Staveley, L.A.K.,
The Densities of Liquid Argon, Krypton, Xenon, Oxygen, Nitrogen, Carbon Monoxide, Methane and Carbon Tetrafluoride Along the Orthobaric Liquid Curve,
J. Chem. Thermodyn., 1969, 1, 413. [all data]
Vogt and Pitzer, 1976
Vogt, G.J.; Pitzer, K.S.,
Entropy and heat capacity of methane, spin-species conversion,
J. Chem. Thermodynam., 1976, 8, 1011-1031. [all data]
Frank and Clusius, 1937
Frank, A.; Clusius, K.,
The entropy of methane,
Z. Physik. Chem., 1937, B36, 291-300. [all data]
Stock, Henning, et al., 2006
Stock, Alfred; Henning, Fritz; Kuß, Ernst,
Dampfdrucktafeln für Temperaturbestimmungen zwischen + 25° und - 185°,
Ber. dtsch. Chem. Ges. A/B, 2006, 54, 5, 1119-1129, https://doi.org/10.1002/cber.19210540531
. [all data]
Boublik, Fried, et al., 1984
Boublik, T.; Fried, V.; Hala, E.,
The Vapour Pressures of Pure Substances: Selected Values of the Temperature Dependence of the Vapour Pressures of Some Pure Substances in the Normal and Low Pressure Region, 2nd ed., Elsevier, New York, 1984, 972. [all data]
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 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]
Ott, Goates, et al., 1972
Ott, J. Bevan; Goates, J. Rex; Lamb, John D.,
Solid-liquid phase equilibria in water + ethylene glycol,
The Journal of Chemical Thermodynamics, 1972, 4, 1, 123-126, https://doi.org/10.1016/S0021-9614(72)80015-6
. [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]
Ambrose, Counsell, et al., 1970
Ambrose, D.; Counsell, J.F.; Davenport, A.J.,
The use of Chebyshev polynomials for the representation of vapour pressures between the triple point and the critical point,
The Journal of Chemical Thermodynamics, 1970, 2, 2, 283-294, https://doi.org/10.1016/0021-9614(70)90093-5
. [all data]
Hestermans and White, 1961
Hestermans, P.; White, David,
THE VAPOR PRESSURE, HEAT OF VAPORIZATION AND HEAT CAPACITY OF METHANE FROM THE BOILING POINT TO THE CRITICAL TEMPERATURE,
J. Phys. Chem., 1961, 65, 2, 362-365, https://doi.org/10.1021/j100820a044
. [all data]
Frank and Clusius, 1939
Frank, A.; Clusius, K.,
Z. Phys. Chem. Abt. B, 1939, 42, 395. [all data]
Prydz and Goodwin, 1972
Prydz, R.; Goodwin, R.D.,
Experimental Melting and Vapor Pressures of Methane,
J. Chem. Thermodyn., 1972, 4, 1, 127-133, https://doi.org/10.1016/S0021-9614(72)80016-8
. [all data]
Regnier, 1972
Regnier, J.,
Tension de Vapeur de L'Ethane Entre 80 et 135 K,
J. Chim. Phys., 1972, 69, 942-944. [all data]
Cutler and Morrison, 1965
Cutler, A.J.B.; Morrison, J.A.,
Excess Thermodynamic Functions for Liquid Mixtures of Methane+Propane,
Trans. Faraday Soc., 1965, 61, 429-442, https://doi.org/10.1039/tf9656100429
. [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]
Armstrong, Brickwedde, et al., 1955
Armstrong, George T.; Brickwedde, F.G.; Scott, R.B.,
Vapor pressures of the methanes,
J. RES. NATL. BUR. STAN., 1955, 55, 1, 39, https://doi.org/10.6028/jres.055.005
. [all data]
Jones, 1960
Jones, A.H.,
Sublimation Pressure Data for Organic Compounds.,
J. Chem. Eng. Data, 1960, 5, 2, 196-200, https://doi.org/10.1021/je60006a019
. [all data]
Tickner and Lossing, 1951
Tickner, A.W.; Lossing, F.P.,
The Measurement of Low Vapor Pressures by Means of a Mass Spectrometer.,
J. Phys. Chem., 1951, 55, 5, 733-740, https://doi.org/10.1021/j150488a013
. [all data]
Stull, 1947
Stull, Daniel R.,
Vapor Pressure of Pure Substances. Organic and Inorganic Compounds,
Ind. Eng. Chem., 1947, 39, 4, 517-540, https://doi.org/10.1021/ie50448a022
. [all data]
Ellison, Engelking, et al., 1978
Ellison, G.B.; Engelking, P.C.; Lineberger, W.C.,
An experimental determination of the geometry and electron affinity of CH3,
J. Am. Chem. Soc., 1978, 100, 2556. [all data]
Graul and Squires, 1990
Graul, S.T.; Squires, R.R.,
Gas-Phase Acidities Derived from Threshold Energies for Activated Reactions,
J. Am. Chem. Soc., 1990, 112, 7, 2517, https://doi.org/10.1021/ja00163a007
. [all data]
Bohme, Lee-Ruff, et al., 1972
Bohme, D.K.; Lee-Ruff, E.; Young, L.B.,
Acidity order of selected bronsted acids in the gas phase at 300K,
J. Am. Chem. Soc., 1972, 94, 5153. [all data]
Check, Faust, et al., 2001
Check, C.E.; Faust, T.O.; Bailey, J.M.; Wright, B.J.; Gilbert, T.M.; Sunderlin, L.S.,
Addition of Polarization and Diffuse Functions to the LANL2DZ Basis Set for P-Block Elements,
J. Phys. Chem. A,, 2001, 105, 34, 8111, https://doi.org/10.1021/jp011945l
. [all data]
Hiraoka and Mori, 1989
Hiraoka, K.; Mori, T.,
Gas - Phase Stability and Structure of Cluster Ions CH5+(CH4)n with n = 1 - 9,
Chem. Phys. Lett., 1989, 161, 2, 111, https://doi.org/10.1016/0009-2614(89)85040-7
. [all data]
Hiraoka and Kebarle, 1975
Hiraoka, K.; Kebarle, P.,
Energetics, Stabilities and Possible Structures of CH5+(CH4)n Clusters from Gas Phase Study of Equilibria CH5+(CH4)n - 1 + CH4 = CH5+(CH4)n for n = 1 - 5,
J. Am. Chem. Soc., 1975, 97, 15, 4179, https://doi.org/10.1021/ja00848a005
. [all data]
Field and Beggs, 1971
Field, F.H.; Beggs, D.P.,
Reversible Reactions of Gas Phase Ions. III. Studies with Methane at 0.1-1.0 Torr and 77-300 K,
J. Am. Chem. Soc., 1971, 93, 7, 1585, https://doi.org/10.1021/ja00736a003
. [all data]
Hiraoka, Mori, et al., 1993
Hiraoka, K.; Mori, T.; Yamabe, S.,
The Gas-Phase Solvation of C2H5+, s-C3H7+ and s-C4H9+ with CH4. The Isomeric Structures of C2H5+ and C2H5+.CH4,
Chem. Phys. Lett., 1993, 207, 2-3, 178, https://doi.org/10.1016/0009-2614(93)87011-Q
. [all data]
Hiroka and Kebarle, 1975
Hiroka, K.; Kebarle, P.,
Information on the Proton Affinity and Protolysis of Propane from Measurement of the Ion Cluster Equilibrium: C2H5+ + CH4 = C3H9+,
Can. J. Phys., 1975, 53, 970. [all data]
Kemper, Bushnell, et al., 1993
Kemper, P.R.; Bushnell, J.; Von Koppen, P.; Bowers, M.T.,
Binding Energies of Co+(H2/CH4/C2H6)1,2,3 Clusters,
J. Phys. Chem., 1993, 97, 9, 1810, https://doi.org/10.1021/j100111a016
. [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]
Haynes and Armentrout, 1996
Haynes, C.L.; Armentrout, P.B.,
Guided Ion Beam Determination of the Co+ - H2 Bond Dissociation energy,
Chem Phys. Let., 1996, 249, 1-2, 64, https://doi.org/10.1016/0009-2614(95)01337-7
. [all data]
Kemper, Bushnell, et al., 1993, 2
Kemper, P.R.; Bushnell, J.; Von Helden, G.; Bowers, M.T.,
Co+(H2)n Clusters: Binding Energies and Molecular Parameters,
J. Chem Phys., 1993, 97, 1, 52, https://doi.org/10.1021/j100103a012
. [all data]
Martinho Simões and Beauchamp, 1990
Martinho Simões, J.A.; Beauchamp, J.L.,
Chem. Rev., 1990, 90, 629. [all data]
Holm, 1981
Holm, T.,
J. Chem. Soc., Perkin Trans. II, 1981, 464.. [all data]
Pedley, 1994
Pedley, J.B.,
Thermodynamic Data and Structures of Organic Compounds; Thermodynamics Research Center Data Series, Vol I, Thermodynamics Research Center, College Station, 1994. [all data]
Martin and Finke, 1990
Martin, B.D.; Finke, R.G.,
J. Am. Chem. Soc., 1990, 112, 2419. [all data]
Martin and Finke, 1992
Martin, B.D.; Finke, R.G.,
J. Am. Chem. Soc., 1992, 114, 585. [all data]
Hiraoka and Kebarle, 1976
Hiraoka, K.; Kebarle, P.,
Stabilities and Energetics of Pentacoordinated Carbonium Ions. The Isomeric C2H7+ Ions and Some Higher Analogues: C3H9+ and C4H11+,
J. Am. Chem. Soc., 1976, 98, 20, 6119, https://doi.org/10.1021/ja00436a009
. [all data]
Golden, Walsh, et al., 1965
Golden, D.M.; Walsh, R.; Benson, S.W.,
The thermochemistry of the gas phase equilibrium I2 + CH4 «=» CH3I + HI and the heat of formation of the methyl radical,
J. Am. Chem. Soc., 1965, 87, 4053-4057. [all data]
Goy and Pritchard, 1965
Goy, C.A.; Pritchard, H.O.,
Kinetics and thermodynamics of the reaction between iodine and methane and the heat of formation of methyl iodide,
J. Phys. Chem., 1965, 69, 3040-3041. [all data]
Nichol and Ubbelohde, 1952
Nichol, R.J.; Ubbelohde, A.R.,
A thermochemical evaluation of bond strengths in some carbon compounds. part II. Bond strengths based on the reaction CH3I + HI = CH4 + I2,
J. Am. Chem. Soc., 1952, 415-421. [all data]
Bennet and Field, 1972
Bennet, S.L.; Field, F.H.,
Reversible Reactions of Gaseous Ions. V. The Methane - Water System at Low Temperatures,
J. Am. Chem. Soc., 1972, 94, 15, 5188, https://doi.org/10.1021/ja00770a008
. [all data]
Bennet and Field, 1972, 2
Bennet, S.L.; Field, F.H.,
Reversible Reactions of Gaseous Ions. VI. The NH3 - CH4, H2S - CH4 and CF4 - CH4 Systems at Low Temperatures,
J. Am. Chem. Soc., 1972, 94, 18, 6305, https://doi.org/10.1021/ja00773a009
. [all data]
Holm, 1974
Holm, T.,
J. Organometal. Chem., 1974, 77, 27. [all data]
Pedley and Rylance, 1977
Pedley, J.B.; Rylance, J.,
Computer Analysed Thermochemical Data: Organic and Organometallic Compounds, University of Sussex, Brigton, 1977. [all data]
Liebman, Martinho Simões, et al., 1995
Liebman, J.F.; Martinho Simões, J.A.; Slayden, S.W.,
In Lithium Chemistry: A Theoretical and Experimental Overview Wiley: New York, Sapse, A.-M.; Schleyer, P. von Ragué, ed(s)., 1995. [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]
Carson, Hartley, et al., 1949
Carson, A.S.; Hartley, K.; Skinner, H.A.,
Thermochemistry of metal alkyls. Part II.?The bond dissociation energies of some Zn?C and Cd?C bonds, and of Et?I.,
Trans. Faraday Soc., 1949, 45, 1159, https://doi.org/10.1039/tf9494501159
. [all data]
Cox and Pilcher, 1970, 2
Cox, J.D.; Pilcher, G.,
Thermochemistry of Organic and Organometallic Compounds
in Academic Press, New York, 1970. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Pc Critical pressure Ptriple Triple point pressure S°gas Entropy of gas at standard conditions S°gas,1 bar Entropy of gas at standard conditions (1 bar) T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature 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 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 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.