Nitric acid
- Formula: HNO3
- Molecular weight: 63.0128
- IUPAC Standard InChIKey: GRYLNZFGIOXLOG-UHFFFAOYSA-N
- CAS Registry Number: 7697-37-2
- Chemical structure:
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Gas phase thermochemistry data
Go To: Top, Phase change data, Reaction thermochemistry 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.
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -32.101 | kcal/mol | Review | Chase, 1998 | Data last reviewed in June, 1963 |
Quantity | Value | Units | Method | Reference | Comment |
S°gas,1 bar | 63.669 | cal/mol*K | Review | Chase, 1998 | Data last reviewed in June, 1963 |
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.
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Temperature (K) | 298. to 1200. | 1200. to 6000. |
---|---|---|
A | 4.692230 | 23.29340 |
B | 36.79730 | 1.297701 |
C | -27.68590 | -0.246101 |
D | 7.858402 | 0.016241 |
E | -0.059540 | -2.938131 |
F | -35.10559 | -46.00650 |
G | 59.20289 | 82.17139 |
H | -32.09990 | -32.09990 |
Reference | Chase, 1998 | Chase, 1998 |
Comment | Data last reviewed in June, 1963 | Data last reviewed in June, 1963 |
Phase change data
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry 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: William E. Acree, Jr., James S. Chickos
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
9.23 | 312. | Holeci, 1966 | Based on data from 273. to 356. K. |
Reaction thermochemistry 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 as indicated in comments:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
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.
Individual Reactions
By formula: (NO3- • HNO3) + HNO3 = (NO3- • 2HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.3 ± 1.0 | kcal/mol | TDAs | Davidson, Fehsenfeld, et al., 1977 | gas phase; B,M |
ΔrH° | 16.00 ± 0.80 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B,M |
ΔrH° | 18.4 | kcal/mol | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
ΔrH° | 17.7 | kcal/mol | HPMS | Lee, Keesee, et al., 1980 | gas phase; M |
ΔrH° | 20.0 | kcal/mol | ATM | Arnold and Qiu, 1984 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
ΔrS° | 22.1 | cal/mol*K | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; M |
ΔrS° | 25. | cal/mol*K | N/A | Arnold and Qiu, 1984 | gas phase; Entropy change calculated or estimated; M |
ΔrS° | 23.1 | cal/mol*K | HPMS | Wlodek, Luczynski, et al., 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 11.7 ± 2.2 | kcal/mol | TDAs | Davidson, Fehsenfeld, et al., 1977 | gas phase; B,M |
ΔrG° | 9.00 ± 0.30 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
12.6 | 233. | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
13.8 | 250. | ATM | Arnold and Qiu, 1984 | gas phase; Entropy change calculated or estimated; M |
By formula: (NO3- • 2HNO3) + HNO3 = (NO3- • 3HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.1 ± 1.0 | kcal/mol | TDAs | Davidson, Fehsenfeld, et al., 1977 | gas phase; B,M |
ΔrH° | 13.9 ± 1.4 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B,M |
ΔrH° | 16.0 | kcal/mol | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
ΔrH° | 16.0 | kcal/mol | HPMS | Lee, Keesee, et al., 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
ΔrS° | 28.9 | cal/mol*K | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; M |
ΔrS° | 26.7 | cal/mol*K | HPMS | Wlodek, Luczynski, et al., 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 7.4 ± 2.2 | kcal/mol | TDAs | Davidson, Fehsenfeld, et al., 1977 | gas phase; B |
ΔrG° | 5.90 ± 0.40 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B |
ΔrG° | 6.9 | kcal/mol | FA | Fehsenfeld, Howard, et al., 1975 | gas phase; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
10.2 | 233. | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 324.50 ± 0.20 | kcal/mol | TDEq | Davidson, Fehsenfeld, et al., 1977 | gas phase; Relative to HBr, reevaluated with current HBr acidity. Excited state at 3.0 eV,81WU /TIE.; B |
ΔrH° | 329.9 ± 4.8 | kcal/mol | NBAE | Mathur, Rothe, et al., 1976 | gas phase; From HNO3; B |
ΔrH° | 329.1 ± 5.8 | kcal/mol | Endo | Refaey and Franklin, 1976 | gas phase; I- + HNO3 ->.; B |
ΔrH° | 324.50 ± 0.50 | kcal/mol | TDEq | Ferguson, Dunkin, et al., 1972 | gas phase; B |
ΔrH° | 356.30 | kcal/mol | Endo | Berkowitz, Chupka, et al., 1971 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 317.80 ± 0.20 | kcal/mol | TDEq | Davidson, Fehsenfeld, et al., 1977 | gas phase; Relative to HBr, reevaluated with current HBr acidity. Excited state at 3.0 eV,81WU /TIE.; B |
By formula: (Br- • HNO3) + HNO3 = (Br- • 2HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.1 | kcal/mol | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; From thermochemical cycle(Br-/NO3- - HNO3/HBr), Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 23.6 | cal/mol*K | N/A | Davidson, Fehsenfeld, et al., 1977 | gas phase; From thermochemical cycle(Br-/NO3- - HNO3/HBr), Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 11.1 | kcal/mol | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; From thermochemical cycle(Br-/NO3- - HNO3/HBr), Entropy change calculated or estimated; M |
By formula: Br- + HNO3 = (Br- • HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20.0 | kcal/mol | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; From thermochemical cycle,switching reaction(Br-/NO3-HNO3/HBr), ΔrH>; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 18.5 | cal/mol*K | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; From thermochemical cycle,switching reaction(Br-/NO3-HNO3/HBr), ΔrH>; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
13.4 | 367. | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; From thermochemical cycle,switching reaction(Br-/NO3-HNO3/HBr), ΔrH>; M |
By formula: (NO3- • HNO3) + H2O = (NO3- • H2O • HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13.0 | kcal/mol | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
7.3 | 233. | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
By formula: (HO4S- • 2H2O4S) + HNO3 = (HO4S- • HNO3 • 2H2O4S)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.9 | kcal/mol | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
10.3 | 233. | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
By formula: (HO4S- • 3H2O4S) + HNO3 = (HO4S- • HNO3 • 3H2O4S)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.9 | kcal/mol | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
11.1 | 233. | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
(HO4S- • ) + HO3S = (HO4S- • HO3S • )
By formula: (HO4S- • HNO3) + HO3S = (HO4S- • HO3S • HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 21.7 | kcal/mol | ATM | Arnold and Qiu, 1984 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Arnold and Qiu, 1984 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
15.5 | 250. | ATM | Arnold and Qiu, 1984 | gas phase; Entropy change calculated or estimated; M |
By formula: (HO4S- • HNO3) + H2O = (HO4S- • H2O • HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13.0 | kcal/mol | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
7.2 | 233. | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
By formula: (HO4S- • HNO3) + HNO3 = (HO4S- • 2HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.4 | kcal/mol | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
12.6 | 233. | ATM | Arnold, Viggiano, et al., 1982 | gas phase; Entropy change calculated or estimated; M |
By formula: (NO3- • 3HNO3) + HNO3 = (NO3- • 4HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.3 ± 1.3 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 19.9 | cal/mol*K | HPMS | Wlodek, Luczynski, et al., 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 3.20 ± 0.40 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B |
ΔrG° | 6.9 ± 1.0 | kcal/mol | IMRE | Fehsenfeld, Howard, et al., 1975 | gas phase; B |
By formula: (NO3- • HNO3) + HBr = (NO3- • HBr • HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.0 | kcal/mol | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; switching reaction(NO3-)2HNO3; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22.9 | cal/mol*K | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; switching reaction(NO3-)2HNO3; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 9.2 | kcal/mol | FA | Davidson, Fehsenfeld, et al., 1977 | gas phase; switching reaction(NO3-)2HNO3; M |
By formula: (NO3- • 5HNO3) + HNO3 = (NO3- • 6HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 4.60 ± 0.90 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 7.3 | cal/mol*K | HPMS | Wlodek, Luczynski, et al., 1980 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 2.40 ± 0.70 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B |
By formula: (NO3- • 4HNO3) + HNO3 = (NO3- • 5HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 7.4 ± 1.2 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 18.6 | cal/mol*K | HPMS | Wlodek, Luczynski, et al., 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1.9 ± 1.0 | kcal/mol | TDAs | Wlodek, Luczynski, et al., 1980 | gas phase; B |
By formula: (NO3- • HBr) + HNO3 = (NO3- • HNO3 • HBr)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.0 ± 2.0 | kcal/mol | TDEq | Davidson, Fehsenfeld, et al., 1977 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 9.6 ± 2.8 | kcal/mol | TDEq | Davidson, Fehsenfeld, et al., 1977 | gas phase; B |
By formula: C3H6N2O7 + HNO3 = C3H5N3O9 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -1.4 ± 0.3 | kcal/mol | Eqk | Kazakov, Kirpichev, et al., 1990 | liquid phase; Heat of nitration; ALS |
ΔrH° | -1.3 ± 0.3 | kcal/mol | Cm | Kazakov, Lagodzinskaya, et al., 1989 | liquid phase; ALS |
By formula: C3H8O3 + HNO3 = C3H7NO5 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -4.5 ± 0.5 | kcal/mol | Eqk | Kazakov, Kirpichev, et al., 1990 | liquid phase; Heat of Nitration; ALS |
ΔrH° | -2.39 | kcal/mol | Cm | Tsvetkov, Sopin, et al., 1986 | liquid phase; ALS |
By formula: NO3- + HNO3 = (NO3- • HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 24. | cal/mol*K | N/A | Davidson, Fehsenfeld, et al., 1977 | gas phase; Entropy change calculated or estimated, DG>, ΔrH>; M |
By formula: Na+ + HNO3 = (Na+ • HNO3)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20.6 | kcal/mol | FA | Perry, Rowe, et al., 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20.3 | cal/mol*K | FA | Perry, Rowe, et al., 1980 | gas phase; M |
By formula: C3H7NO5 + HNO3 = C3H6N2O7 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.7 ± 0.7 | kcal/mol | Eqk | Kazakov, Kirpichev, et al., 1990 | liquid phase; Heat of nitration; ALS |
By formula: C3H8O3 + HNO3 = C3H7NO5 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -2.5 ± 0.6 | kcal/mol | Eqk | Kazakov, Kirpichev, et al., 1990 | liquid phase; Heat of nitration; ALS |
By formula: C3H6N2O7 + H2O = C3H7NO5 + HNO3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.7 ± 0.6 | kcal/mol | Eqk | Kazakov, Kirpichev, et al., 1990 | liquid phase; Heat of nitration; ALS |
By formula: C3H6N2O7 + HNO3 = C3H5N3O9 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -2.5 ± 0.3 | kcal/mol | Eqk | Kazakov, Kirpichev, et al., 1990 | liquid phase; Heat of nitration; ALS |
By formula: C3H7NO5 + 2HNO3 = C3H5N3O9 + 2H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -4.2 ± 0.3 | kcal/mol | Cm | Kazakov, Lagodzinskaya, et al., 1989 | liquid phase; ALS |
By formula: C3H8O3 + 3HNO3 = C3H5N3O9 + 3H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -8.7 ± 0.4 | kcal/mol | Cm | Kazakov, Lagodzinskaya, et al., 1989 | liquid phase; ALS |
By formula: C4H10O3 + HNO3 = C4H9NO5 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -2.70 | kcal/mol | Cm | Tsvetkov, Sopin, et al., 1986 | liquid phase; ALS |
By formula: CH3NO2 + HNO3 = 2NO2 + CH4O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.89 | kcal/mol | Eqk | Silverwood and Thomas, 1967 | gas phase; ALS |
+ = C2F3NO4 +
By formula: C4F6O3 + HNO3 = C2F3NO4 + C2HF3O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -6.60 | kcal/mol | Cm | Tsvetkov, Shmakov, et al., 1989 | liquid phase; ALS |
+ = C5H11NO6 +
By formula: C5H12O4 + HNO3 = C5H11NO6 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.70 | kcal/mol | Cm | Tsvetkov, Sopin, et al., 1986 | liquid phase; ALS |
By formula: C2H6O2 + HNO3 = C2H5NO4 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -1.9 | kcal/mol | Cm | Tsvetkov, Sopin, et al., 1986 | liquid phase; ALS |
By formula: C4H10O3 + HNO3 = C4H9NO5 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -2.1 | kcal/mol | Cm | Tsvetkov, Sopin, et al., 1986 | liquid phase; ALS |
By formula: C2H3NO4 + C2H4O2 = C4H6O3 + HNO3
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.99 | kcal/mol | Cm | Tsvetkov, Shmakov, et al., 1989 | liquid phase; ALS |
By formula: C3H8O + HNO3 = C3H7NO3 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -5.59 | kcal/mol | Eqk | Rubtsov, 1986 | liquid phase; ALS |
By formula: CH4O + HNO3 = CH3NO3 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -6.60 | kcal/mol | Eqk | Rubtsov, 1986 | liquid phase; ALS |
By formula: C2H6O + HNO3 = C2H5NO3 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -6.00 | kcal/mol | Eqk | Rubtsov, 1986 | liquid phase; ALS |
By formula: C3H8O + HNO3 = C3H7NO3 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -5.21 | kcal/mol | Eqk | Rubtsov, 1986 | liquid phase; ALS |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: 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 |
---|---|---|---|---|
210000. | 8700. | R | N/A | missing citation assume the temperature dependence to be the same as for a(H+) a(NO3-) / p(HNO3) in missing citation. |
2.4×10+6/KA | 8700. | T | N/A | For strong acids, the solubility is often expressed as kH = ([H+] * [A-]) / p(HA). To obtain the physical solubility of HA, the value has to be divided by the acidity constant KA. missing citation corrects erroneous data from missing citation. |
2.6×10+6 | 8700. | T | N/A | |
350000./KA | 8700. | Q | N/A | For strong acids, the solubility is often expressed as kH = ([H+] * [A-]) / p(HA). To obtain the physical solubility of HA, the value has to be divided by the acidity constant KA. missing citation refer to several references in their list of Henry's law constants but they don't assign them to specific species. |
89000. | C | N/A | ||
210000. | T | N/A |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law 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]
Holeci, 1966
Holeci, I.,
Chem. Prum., 1966, 16, 5, 267. [all data]
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Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, References
- Symbols used in this document:
S°gas,1 bar Entropy of gas at standard conditions (1 bar) T Temperature d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K 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 ΔvapH Enthalpy of vaporization - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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