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.
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Gas phase thermochemistry data
Go To: Top, Phase change data, Henry's Law data, Gas phase ion energetics 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, Henry's Law data, Gas phase ion energetics 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)
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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)
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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 |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Phase change data, Gas phase ion energetics 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: 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 |
---|---|---|---|---|
0.0014 | 1600. | L | N/A | The parameterization given by missing citation (parameters A, B, C) doesn't fit the data in the same paper for this substance. Therefore the parameteriztaion of the solubility data (X1) was recalculated. |
0.0013 | 1900. | Q | N/A | Only the tabulated data between T = 273. K and T = 303. K from missing citation was used to derive kH and -Δ kH/R. Above T = 303. K the tabulated data could not be parameterized by equation (reference missing) very well. The partial pressure of water vapor (needed to convert some Henry's law constants) was calculated using the formula given by missing citation. The quantities A and α from missing citation were assumed to be identical. |
0.0015 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.0013 | L | N/A | ||
0.0013 | 1800. | X | N/A | |
0.0014 | 1700. | L | N/A | |
0.0015 | V | N/A | ||
0.00097 | C | N/A | ||
0.0014 | R | N/A | ||
0.0092 | V | N/A |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
View reactions leading to CH4+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 12.61 ± 0.01 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 129.9 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 124.4 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
Appearance energy determinations
De-protonation reactions
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 |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics 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,
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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,
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Halford J.O., 1957
Halford J.O.,
Standard heat capacities of gaseous methanol, ethanol, methane and ethane at 279 K by thermal conductivity,
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McDowell R.S., 1963
McDowell R.S.,
Thermodynamic functions of methane,
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Streng, 1971
Streng, A.G.,
Miscibility and Compatibility of Some Liquid and Solidified Gases at Low Temperature,
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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.,
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Timmermans, 1935
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Researches in Stoichiometry. I. The Heat of Fusion of Organic Compounds.,
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Clusius, 1929
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The specific heat of several condensed gases between 10deg. abs. and their triple point.,
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Eucken and Karwat, 1924
Eucken, A.; Karwat, E.,
Determination of the heat content of several condensed gases,
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Ambrose and Tsonopoulos, 1995
Ambrose, D.; Tsonopoulos, C.,
Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkenes,
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Younglove and Ely, 1987
Younglove, B.A.; Ely, J.F.,
Thermophysical Properties of Fluids II. Methane, Ethane, Propane, Isobutane, and Normal Butane,
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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,
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Vogt and Pitzer, 1976
Vogt, G.J.; Pitzer, K.S.,
Entropy and heat capacity of methane, spin-species conversion,
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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°,
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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,
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. [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,
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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,
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. [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,
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. [all data]
Frank and Clusius, 1939
Frank, A.; Clusius, K.,
Z. Phys. Chem. Abt. B, 1939, 42, 395. [all data]
Prydz and Goodwin, 1972
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Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas IE (evaluated) Recommended ionization energy 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) Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy 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
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