Hydrogen
- Formula: H2
- Molecular weight: 2.01588
- IUPAC Standard InChIKey: UFHFLCQGNIYNRP-UHFFFAOYSA-N
- CAS Registry Number: 1333-74-0
- 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: Dihydrogen; o-Hydrogen; p-Hydrogen; Molecular hydrogen; H2; UN 1049; UN 1966
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Reaction thermochemistry data: reactions 1 to 50, reactions 51 to 100, reactions 101 to 150, reactions 151 to 200, reactions 201 to 250, reactions 251 to 300, reactions 301 to 350, reactions 351 to 400, reactions 401 to 450, reactions 451 to 500, reactions 501 to 550, reactions 551 to 600, reactions 601 to 621
- Gas phase ion energetics data
- Mass spectrum (electron ionization)
- Constants of diatomic molecules
- Fluid Properties
- Data at other public NIST sites:
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Gas phase thermochemistry data
Go To: Top, Phase change data, Henry's Law data, Ion clustering data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°gas,1 bar | 130.680 ± 0.003 | J/mol*K | Review | Cox, Wagman, et al., 1984 | CODATA Review value |
S°gas,1 bar | 130.68 | J/mol*K | Review | Chase, 1998 | Data last reviewed in March, 1977 |
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 (J/mol*K)
H° = standard enthalpy (kJ/mol)
S° = standard entropy (J/mol*K)
t = temperature (K) / 1000.
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Temperature (K) | 298. to 1000. | 1000. to 2500. | 2500. to 6000. |
---|---|---|---|
A | 33.066178 | 18.563083 | 43.413560 |
B | -11.363417 | 12.257357 | -4.293079 |
C | 11.432816 | -2.859786 | 1.272428 |
D | -2.772874 | 0.268238 | -0.096876 |
E | -0.158558 | 1.977990 | -20.533862 |
F | -9.980797 | -1.147438 | -38.515158 |
G | 172.707974 | 156.288133 | 162.081354 |
H | 0.0 | 0.0 | 0.0 |
Reference | Chase, 1998 | Chase, 1998 | Chase, 1998 |
Comment | Data last reviewed in March, 1977; New parameter fit October 2001 | Data last reviewed in March, 1977; New parameter fit October 2001 | Data last reviewed in March, 1977; New parameter fit October 2001 |
Phase change data
Go To: Top, Gas phase thermochemistry data, Henry's Law data, Ion clustering data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Ttriple | 0. | K | N/A | Roder, Childs, et al., 1973 | TRC |
Ttriple | 13.95 | K | N/A | Clusius and Weigand, 1940 | Uncertainty assigned by TRC = 0.06 K; see property X for dP/dT for c-l equil.; TRC |
Ttriple | 13.96 | K | N/A | Henning and Otto, 1936 | Uncertainty assigned by TRC = 0.05 K; temperature measured with He gas thermometer; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 0. | bar | N/A | Roder, Childs, et al., 1973 | TRC |
Ptriple | 0.0721 | bar | N/A | Henning and Otto, 1936 | Uncertainty assigned by TRC = 0.0004 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 33.18 | K | N/A | Onnes, Crommelin, et al., 1917 | Uncertainty assigned by TRC = 0.2 K; derived from P-V-T measurements; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 13.00 | bar | N/A | Onnes, Crommelin, et al., 1917 | Uncertainty assigned by TRC = 0.0119 bar; derived from vapor pressure extrapolated to Tc; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 15.4 | mol/l | N/A | Onnes, Crommelin, et al., 1917 | Uncertainty assigned by TRC = 2. mol/l; by extrapolation of rectilinear diameter to Tc; TRC |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
21.01 to 32.27 | 3.54314 | 99.395 | 7.726 | van Itterbeek, Verbeke, et al., 1964 | Coefficents calculated by NIST from author's data. |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Phase change data, Ion clustering data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled 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 |
---|---|---|---|---|
0.00078 | 500. | L | N/A | |
0.00078 | 640. | 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. |
0.00078 | 490. | L | N/A | |
0.00078 | R | N/A |
Ion clustering 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 compiled by: Michael M. Meot-Ner (Mautner) and Sharon G. Lias
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. Searches may be limited to ion clustering reactions. A general reaction search form is also available.
Clustering reactions
By formula: Ar+ + H2 = (Ar+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 93.7 | kJ/mol | FA | Shul, Passarella, et al., 1987 | gas phase; switching reaction(Ar+)Ar, ΔrH>; Dehmer and Pratt, 1982 |
By formula: CHO+ + H2 = (CHO+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16. | kJ/mol | PHPMS | Hiraoka and Kebarle, 1975 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 85.8 | J/mol*K | PHPMS | Hiraoka and Kebarle, 1975 | gas phase |
By formula: CH5+ + H2 = (CH5+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 7.87 ± 0.42 | kJ/mol | PHPMS | Hiraoka, Kudaka, et al., 1991 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 50.6 | J/mol*K | PHPMS | Hiraoka, Kudaka, et al., 1991 | gas phase |
By formula: (CH5+ • H2) + H2 = (CH5+ • 2H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 7.45 ± 0.42 | kJ/mol | PHPMS | Hiraoka, Kudaka, et al., 1991 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 67.8 | J/mol*K | PHPMS | Hiraoka, Kudaka, et al., 1991 | gas phase |
By formula: (CH5+ • 2H2) + H2 = (CH5+ • 3H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.74 ± 0.42 | kJ/mol | PHPMS | Hiraoka, Kudaka, et al., 1991 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 94.6 | J/mol*K | PHPMS | Hiraoka, Kudaka, et al., 1991 | gas phase |
By formula: (CH5+ • 3H2) + H2 = (CH5+ • 4H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.57 ± 0.42 | kJ/mol | PHPMS | Hiraoka, Kudaka, et al., 1991 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 108. | J/mol*K | PHPMS | Hiraoka, Kudaka, et al., 1991 | gas phase |
By formula: C3H7+ + H2 = (C3H7+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10. | kJ/mol | PHPMS | Hiraoka and Kebarle, 1976 | gas phase; Entropy change calculated or estimated, DG<, ΔrH< |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 84. | J/mol*K | N/A | Hiraoka and Kebarle, 1976 | gas phase; Entropy change calculated or estimated, DG<, ΔrH< |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
4. | 170. | PHPMS | Hiraoka and Kebarle, 1976 | gas phase; Entropy change calculated or estimated, DG<, ΔrH< |
By formula: (Co+ • CH4) + H2 = (Co+ • H2 • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 95.8 | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2H2, ΔrS(440 K); Kemper, Bushnell, et al., 1993, 2 |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
73. (+3.,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2H2, ΔrS(440 K); Kemper, Bushnell, et al., 1993, 2 |
By formula: (Co+ • H2O) + H2 = (Co+ • H2 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 103. | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(530 K) |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
83. (+3.,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(530 K) |
By formula: Co+ + H2 = (Co+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 82. ± 4. | kJ/mol | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(O K)=76.1 kJ/mol, ΔrS(300 K)=86.2 J/mol*K |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 92.0 | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(O K)=76.1 kJ/mol, ΔrS(300 K)=86.2 J/mol*K |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
73.2 (+9.6,-0.) | CID | Haynes and Armentrout, 1996 | gas phase; guided ion beam CID |
By formula: (Co+ • H2) + H2 = (Co+ • 2H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 75. ± 3. | kJ/mol | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=71.1 kJ/mol, ΔrS(300 K)=103. J/mol*K |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 103. | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=71.1 kJ/mol, ΔrS(300 K)=103. J/mol*K |
By formula: (Co+ • 2H2) + H2 = (Co+ • 3H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 44. ± 2. | kJ/mol | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=40. kJ/mol, ΔrS(300 K)=85.8 J/mol*K |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 85.8 | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=40. kJ/mol, ΔrS(300 K)=85.8 J/mol*K |
By formula: (Co+ • 3H2) + H2 = (Co+ • 4H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 44. ± 3. | kJ/mol | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=40. kJ/mol, ΔrS(300 K)=105. J/mol*K |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 101. | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=40. kJ/mol, ΔrS(300 K)=105. J/mol*K |
By formula: (Co+ • 4H2) + H2 = (Co+ • 5H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22. ± 3. | kJ/mol | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=18. kJ/mol, ΔrS(300 K)=91.6 J/mol*K |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 94.1 | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=18. kJ/mol, ΔrS(300 K)=91.6 J/mol*K |
By formula: (Co+ • 5H2) + H2 = (Co+ • 6H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20. ± 3. | kJ/mol | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=17. kJ/mol, ΔrS(300 K)=99.6 J/mol*K |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 99.2 | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=17. kJ/mol, ΔrS(300 K)=99.6 J/mol*K |
By formula: (Co+ • 6H2) + H2 = (Co+ • 7H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6. ± 3. | kJ/mol | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=3. kJ/mol; ΔrS(300 K)=75.3 J/mol*K |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 75.3 | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993, 2 | gas phase; ΔrH(0 K)=3. kJ/mol; ΔrS(300 K)=75.3 J/mol*K |
By formula: Fe+ + H2 = (Fe+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 52.3 ± 0.8 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 45.2 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 90.0 | J/mol*K | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 45.2 kJ/mol |
By formula: (Fe+ • H2) + H2 = (Fe+ • 2H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 71.1 ± 0.8 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 65.7 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 105. | J/mol*K | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 65.7 kJ/mol |
By formula: (Fe+ • 2H2) + H2 = (Fe+ • 3H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 35. ± 0.4 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 31. kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 79.9 | J/mol*K | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 31. kJ/mol |
By formula: (Fe+ • 3H2) + H2 = (Fe+ • 4H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 41. ± 0.4 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 36. kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 104. | J/mol*K | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 36. kJ/mol |
By formula: (Fe+ • 4H2) + H2 = (Fe+ • 5H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11. ± 0.4 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 9.2 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 74.9 | J/mol*K | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 9.2 kJ/mol |
By formula: (Fe+ • 5H2) + H2 = (Fe+ • 6H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11. ± 0.4 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 9.6 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 75.7 | J/mol*K | SIDT | Bushnell, Kemper, et al., 1995 | gas phase; ΔrH(0K) = 9.6 kJ/mol |
By formula: HN2+ + H2 = (HN2+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 30. | kJ/mol | PHPMS | Hiraoka, Saluja, et al., 1979 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 94.6 | J/mol*K | PHPMS | Hiraoka, Saluja, et al., 1979 | gas phase |
By formula: (HN2+ • H2) + H2 = (HN2+ • 2H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 7.5 | kJ/mol | PHPMS | Hiraoka, Saluja, et al., 1979 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 71. | J/mol*K | PHPMS | Hiraoka, Saluja, et al., 1979 | gas phase |
By formula: HO- + H2 = (HO- • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 30. | kJ/mol | CID | Paulson and Henchman, 1984 | gas phase; approximate value |
By formula: HO2+ + H2 = (HO2+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 52.3 | kJ/mol | PHPMS | Hiraoka, Saluja, et al., 1979 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 92. | J/mol*K | PHPMS | Hiraoka, Saluja, et al., 1979 | gas phase |
By formula: (HO2+ • O2) + H2 = (HO2+ • H2 • O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 17. | kJ/mol | PHPMS | Hiraoka, Saluja, et al., 1979 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 71. | J/mol*K | PHPMS | Hiraoka, Saluja, et al., 1979 | gas phase |
By formula: H3+ + H2 = (H3+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 29. ± 2. | kJ/mol | AVG | N/A | Average of 4 out of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 72.8 to 72.8 | J/mol*K | RNG | N/A | Range of 6 values; Individual data points |
By formula: (H3+ • H2) + H2 = (H3+ • 2H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14. ± 0.8 | kJ/mol | PHPMS | Hiraoka, 1987 | gas phase |
ΔrH° | 13. | kJ/mol | HPMS | Beuhler, Ehrenson, et al., 1983 | gas phase |
ΔrH° | 14. | kJ/mol | HPMS | Beuhler, Ehrenson, et al., 1983 | gas phase; deuterated |
ΔrH° | 17. | kJ/mol | PHPMS | Hiraoka and Kebarle, 1975, 2 | gas phase |
ΔrH° | 7.5 | kJ/mol | HPMS | Bennett and Field, 1972 | gas phase; Entropy change is questionable |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 72.8 | J/mol*K | PHPMS | Hiraoka, 1987 | gas phase |
ΔrS° | 70.7 | J/mol*K | HPMS | Beuhler, Ehrenson, et al., 1983 | gas phase |
ΔrS° | 67.4 | J/mol*K | HPMS | Beuhler, Ehrenson, et al., 1983 | gas phase; deuterated |
ΔrS° | 82.8 | J/mol*K | PHPMS | Hiraoka and Kebarle, 1975, 2 | gas phase |
ΔrS° | 45.2 | J/mol*K | HPMS | Bennett and Field, 1972 | gas phase; Entropy change is questionable |
By formula: (H3+ • 2H2) + H2 = (H3+ • 3H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13. ± 0.4 | kJ/mol | PHPMS | Hiraoka, 1987 | gas phase |
ΔrH° | 16. | kJ/mol | PHPMS | Hiraoka and Kebarle, 1975, 2 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 77.4 | J/mol*K | PHPMS | Hiraoka, 1987 | gas phase |
ΔrS° | 84.5 | J/mol*K | PHPMS | Hiraoka and Kebarle, 1975, 2 | gas phase |
By formula: (H3+ • 3H2) + H2 = (H3+ • 4H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 7.2 ± 0.4 | kJ/mol | PHPMS | Hiraoka, 1987 | gas phase |
ΔrH° | 10. | kJ/mol | PHPMS | Hiraoka and Kebarle, 1975, 2 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 74.9 | J/mol*K | PHPMS | Hiraoka, 1987 | gas phase |
ΔrS° | 80.8 | J/mol*K | PHPMS | Hiraoka and Kebarle, 1975, 2 | gas phase |
By formula: (H3+ • 4H2) + H2 = (H3+ • 5H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.9 ± 0.4 | kJ/mol | PHPMS | Hiraoka, 1987 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 79.1 | J/mol*K | PHPMS | Hiraoka, 1987 | gas phase |
By formula: (H3+ • 5H2) + H2 = (H3+ • 6H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.4 ± 0.4 | kJ/mol | PHPMS | Hiraoka, 1987 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 83.7 | J/mol*K | PHPMS | Hiraoka, 1987 | gas phase |
By formula: (H3+ • 6H2) + H2 = (H3+ • 7H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.7 ± 0.4 | kJ/mol | PHPMS | Hiraoka, 1987 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 69.0 | J/mol*K | PHPMS | Hiraoka, 1987 | gas phase |
By formula: (H3+ • 7H2) + H2 = (H3+ • 8H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.3 ± 0.4 | kJ/mol | PHPMS | Hiraoka, 1987 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 74.9 | J/mol*K | PHPMS | Hiraoka, 1987 | gas phase |
By formula: (H3+ • 8H2) + H2 = (H3+ • 9H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 2.6 ± 0.4 | kJ/mol | PHPMS | Hiraoka, 1987 | gas phase |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 79.9 | J/mol*K | PHPMS | Hiraoka, 1987 | gas phase |
By formula: H3O+ + H2 = (H3O+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15. ± 2. | kJ/mol | SCATTERING | Okumura, Yeh, et al., 1990 | gas phase |
By formula: K+ + H2 = (K+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 7.78 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1994 | gas phase; ΔrH(0K) = 6.07 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 56.5 | J/mol*K | SIDT | Bushnell, Kemper, et al., 1994 | gas phase; ΔrH(0K) = 6.07 kJ/mol |
By formula: (K+ • H2) + H2 = (K+ • 2H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.15 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1994 | gas phase; ΔrH(0K) = 5.65 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 46.9 | J/mol*K | SIDT | Bushnell, Kemper, et al., 1994 | gas phase; ΔrH(0K) = 5.65 kJ/mol |
By formula: Li+ + H2 = (Li+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 27. ± 19. | kJ/mol | EI | Wu, 1979 | gas phase |
By formula: Na+ + H2 = (Na+ • H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 12.3 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1994 | gas phase; ΔrH(0K) = 10.3 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 55.2 | J/mol*K | SIDT | Bushnell, Kemper, et al., 1994 | gas phase; ΔrH(0K) = 10.3 kJ/mol |
By formula: (Na+ • H2) + H2 = (Na+ • 2H2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10.1 | kJ/mol | SIDT | Bushnell, Kemper, et al., 1994 | gas phase; ΔrH(0K) = 9.41 kJ/mol |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 51.9 | J/mol*K | SIDT | Bushnell, Kemper, et al., 1994 | gas phase; ΔrH(0K) = 9.41 kJ/mol |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Ion clustering data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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Onnes, H.K.; Crommelin, C.-A.; Cath, P.G.,
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Shul, R.J.; Passarella, R.; Upshulte, B.L.; Keesee, R.G.; Castleman, A.W.,
Thermal Energy Reactions Invoving Ar+ Monomer and Dimer with N2, H2, Xe, and Kr,
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Photoionization of ArKr, ArXe, and KrXe and bond dissociation energies of the rare gas dimer ions,
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Stability and Structure of H3CO+ Formed from COH+ + H2 at Low Temperature,
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Gas-Phase Solvation of CH5+ with H2,
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Hiraoka and Kebarle, 1976
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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,
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Factors Affecting sigma Bond Activation in Simple Systems; Measurement of Experimental Binding energies of Fe+(H2)1-6 Clusters,
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Hiraoka, K.,
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Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Ion clustering data, References
- Symbols used in this document:
Pc Critical pressure Ptriple Triple point pressure S°gas,1 bar Entropy of gas at standard conditions (1 bar) T Temperature Tc Critical temperature Ttriple Triple point temperature d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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