Nitrogen
- Formula: N2
- Molecular weight: 28.0134
- IUPAC Standard InChIKey: IJGRMHOSHXDMSA-UHFFFAOYSA-N
- CAS Registry Number: 7727-37-9
- 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: Nitrogen gas; N2; UN 1066; UN 1977; Dinitrogen; Molecular nitrogen; Diatomic nitrogen; Nitrogen-14
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Gas phase thermochemistry data
Go To: Top, 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.
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°gas,1 bar | 191.609 ± 0.004 | J/mol*K | Review | Cox, Wagman, et al., 1984 | CODATA Review value |
S°gas,1 bar | 191.61 | 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) | 100. to 500. | 500. to 2000. | 2000. to 6000. |
---|---|---|---|
A | 28.98641 | 19.50583 | 35.51872 |
B | 1.853978 | 19.88705 | 1.128728 |
C | -9.647459 | -8.598535 | -0.196103 |
D | 16.63537 | 1.369784 | 0.014662 |
E | 0.000117 | 0.527601 | -4.553760 |
F | -8.671914 | -4.935202 | -18.97091 |
G | 226.4168 | 212.3900 | 224.9810 |
H | 0.0 | 0.0 | 0.0 |
Reference | Chase, 1998 | Chase, 1998 | Chase, 1998 |
Comment | Data last reviewed in March, 1977; New parameter fit January 2009 | Data last reviewed in March, 1977; New parameter fit January 2009 | Data last reviewed in March, 1977; New parameter fit January 2009 |
Phase change data
Go To: Top, Gas phase 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 as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 77.34 | K | N/A | Jacobsen, Stewart, et al., 1986 | TRC |
Tboil | 77.4 | K | N/A | Streng, 1971 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 63.3 | K | N/A | Streng, 1971 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 63.14 | K | N/A | Jacobsen, Stewart, et al., 1986 | TRC |
Ttriple | 63.14 | K | N/A | Angus, de Reuck, et al., 1979 | Uncertainty assigned by TRC = 0.005 K; TRC |
Ttriple | 63.14 | K | N/A | Henning and Otto, 1936 | Uncertainty assigned by TRC = 0.06 K; temperature measured with He gas thermometer; TRC |
Ttriple | 63.13 | K | N/A | Giauque and Clayton, 1933 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.06 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 0.1252 | bar | N/A | Jacobsen, Stewart, et al., 1986 | Uncertainty assigned by TRC = 0.0005 bar; TRC |
Ptriple | 0.1253 | bar | N/A | Angus, de Reuck, et al., 1979 | Uncertainty assigned by TRC = 0.0002 bar; TRC |
Ptriple | 0.126 | bar | N/A | Henning and Otto, 1936 | Uncertainty assigned by TRC = 0.0007 bar; TRC |
Ptriple | 0.1253 | bar | N/A | Giauque and Clayton, 1933 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.0001 bar; Average Pressure; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 126.19 | K | N/A | Jacobsen, Stewart, et al., 1986 | Uncertainty assigned by TRC = 0.01 K; TRC |
Tc | 126.2 | K | N/A | Angus, de Reuck, et al., 1979 | Uncertainty assigned by TRC = 0.05 K; TRC |
Tc | 126.2 | K | N/A | Weber, 1970 | Uncertainty assigned by TRC = 0.2 K; IPTS-68, critical point not observed and Tc taken from literature but equation would allow pc to be calculated. Tc unct. several tenths K. "Ultra-high" purity nitrogen.; TRC |
Tc | 128.45 | K | N/A | Cardoso, 1915 | Uncertainty assigned by TRC = 0.5 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 33.978 | bar | N/A | Jacobsen, Stewart, et al., 1986 | Uncertainty assigned by TRC = 0.007 bar; TRC |
Pc | 34.00 | bar | N/A | Angus, de Reuck, et al., 1979 | Uncertainty assigned by TRC = 0.05 bar; TRC |
Pc | 3.0698 | bar | N/A | Cardoso, 1915 | Uncertainty assigned by TRC = 0.003 bar; TRC |
Pc | 3.0682 | bar | N/A | Cardoso, 1915 | Uncertainty assigned by TRC = 0.003 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 11.18 | mol/l | N/A | Jacobsen, Stewart, et al., 1986 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
ρc | 11.2 | mol/l | N/A | Angus, de Reuck, et al., 1979 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
6.1 | 78. | Edejer and Thodos, 1967 | Based on data from 63. to 126. K.; AC |
5.6 | 77. | Giauque and Clayton, 1933, 2 | AC |
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 |
---|---|---|---|---|---|
63.14 to 126. | 3.7362 | 264.651 | -6.788 | Edejer and Thodos, 1967 | Coefficents calculated by NIST from author's data. |
63.14 to 78.00 | 3.63792 | 257.877 | -6.344 | Moussa, Muijlwijk, et al., 1966 | Coefficents calculated by NIST from author's data. |
Henry's Law 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 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 |
---|---|---|---|
0.00060 | 1300. | X | N/A |
0.00065 | 1300. | L | N/A |
References
Go To: Top, Gas phase thermochemistry data, Phase change 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.
Cox, Wagman, et al., 1984
Cox, J.D.; Wagman, D.D.; Medvedev, V.A.,
CODATA Key Values for Thermodynamics, Hemisphere Publishing Corp., New York, 1984, 1. [all data]
Chase, 1998
Chase, M.W., Jr.,
NIST-JANAF Themochemical Tables, Fourth Edition,
J. Phys. Chem. Ref. Data, Monograph 9, 1998, 1-1951. [all data]
Jacobsen, Stewart, et al., 1986
Jacobsen, R.T.; Stewart, R.B.; Jahangiri, M.,
Termodynamic Properties of Nitrogen from the Freezing Line to 2000 K at Pressures to 1000 MPa,
J. Phys. Chem. Ref. Data, 1986, 15, 735-909. [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]
Angus, de Reuck, et al., 1979
Angus, S.; de Reuck, K.M.; Armstrong, B.; Jacobsen, R.T.; Stewart, R.B.,
International Thermodynamic Tables of the Fluid State - 6 Nitrogen, Pergamon, New York, 1979. [all data]
Henning and Otto, 1936
Henning, F.; Otto, J.,
Vapor pressure curves and triple points in the temperature region from 14 to 90 k,
Phys. Z., 1936, 37, 633-8. [all data]
Giauque and Clayton, 1933
Giauque, W.F.; Clayton, J.O.,
Heat Capacity and Entropy of Nitrogen. Heat of Vaporization. Vapor Pressure of Solid and Liquid. The Reaction 1/2 N2 + 1/2 O2 = NO from Spectroscopic Data,
J. Am. Chem. Soc., 1933, 55, 4875. [all data]
Weber, 1970
Weber, L.A.,
Some vapor pressure and P,V,T data on nitrogen in t he range 65 to 140 K,
J. Chem. Thermodyn., 1970, 2, 839-846. [all data]
Cardoso, 1915
Cardoso, E.,
Study of the Critical Point of Several Difficultly LIquifiable Gases: Nitrogen, Carbon Monoxide, Oxygen and Methane,
J. Chim. Phys. Phys.-Chim. Biol., 1915, 13, 312. [all data]
Edejer and Thodos, 1967
Edejer, Merardo P.; Thodos, George,
Vapor pressures of liquid nitrogen between the triple and critical points,
J. Chem. Eng. Data, 1967, 12, 2, 206-209, https://doi.org/10.1021/je60033a014
. [all data]
Giauque and Clayton, 1933, 2
Giauque, W.F.; Clayton, J.O.,
The Heat Capacity and Entropy of Nitrogen. Heat of Vaporization. Vapor Pressures of Solid and Liquid. The Reaction 1/2 N 2 + 1/2 O 2 = NO from Spectroscopic Data,
J. Am. Chem. Soc., 1933, 55, 12, 4875-4889, https://doi.org/10.1021/ja01339a024
. [all data]
Moussa, Muijlwijk, et al., 1966
Moussa, M.R.; Muijlwijk, R.; van Dijk, H.,
The Vapour Pressure of Liquid Nitrogen,
Physica (Amsterdam), 1966, 32, 5, 900-912, https://doi.org/10.1016/0031-8914(66)90021-8
. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law 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) Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point 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 ΔvapH Enthalpy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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