mercury
- Formula: Hg
- Molecular weight: 200.59
- IUPAC Standard InChIKey: QSHDDOUJBYECFT-UHFFFAOYSA-N
- CAS Registry Number: 7439-97-6
- Chemical structure:
This structure is also available as a 2d Mol file - 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:
- NIST Atomic Spectra Database - Lines Holdings (on physics web site)
- NIST Atomic Spectra Database - Levels Holdings (on physics web site)
- NIST Atomic Spectra Database - Ground states and ionization energies (on physics web site)
- Gas Phase Kinetics Database
- X-ray Photoelectron Spectroscopy Database, version 5.0
- Options:
Data at NIST subscription sites:
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, Condensed phase thermochemistry data, 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 | 61.38 ± 0.04 | kJ/mol | Review | Cox, Wagman, et al., 1984 | CODATA Review value |
ΔfH°gas | 61.38 | kJ/mol | Review | Chase, 1998 | Data last reviewed in December, 1961 |
Quantity | Value | Units | Method | Reference | Comment |
S°gas,1 bar | 174.971 ± 0.005 | J/mol*K | Review | Cox, Wagman, et al., 1984 | CODATA Review value |
S°gas,1 bar | 174.97 | J/mol*K | Review | Chase, 1998 | Data last reviewed in December, 1961 |
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.
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 629.839 to 6000. |
---|---|
A | 20.67243 |
B | 0.179353 |
C | -0.080120 |
D | 0.010547 |
E | 0.007013 |
F | 55.23215 |
G | 199.9797 |
H | 61.38012 |
Reference | Chase, 1998 |
Comment | Data last reviewed in December, 1961 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, 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 |
---|---|---|---|---|---|
S°liquid | 75.90 ± 0.12 | J/mol*K | Review | Cox, Wagman, et al., 1984 | CODATA Review value |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed 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 as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 629.81 | K | N/A | Marsh, 1987 | Uncertainty assigned by TRC = 0.01 K; recommended as fixed point for thermometry; TRC |
Tboil | 629.7 | K | N/A | Honig and Kramer, 1969 | Uncertainty assigned by TRC = 0.5 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 234.3 | K | N/A | Anonymous, 1988 | Uncertainty assigned by TRC = 0.005 K; nominal value, from the catalog; TRC |
Tfus | 234.31 | K | N/A | Marsh, 1987 | Uncertainty assigned by TRC = 0.005 K; TRC |
Tfus | 234.5 | K | N/A | Timmermans, 1911 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 234.3 | K | N/A | Marsh, 1987 | Uncertainty assigned by TRC = 0.003 K; values recommended as calibration standard; TRC |
Ttriple | 234.29 | K | N/A | Honig and Kramer, 1969 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 0. | K | N/A | Menzies, 1913 | based on his observations, author doubts that Tc observed by Koninsberger (1913-170), 1275 deg C is correct; TRC |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
298.14 to 749.99 | 4.85767 | 3007.129 | -10.001 | Hicks, 1963 | Coefficents calculated by NIST from author's data. |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed 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. 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: (Hg+ • 20Hg) + Hg = (Hg+ • 21Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 42.7 | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 21Hg) + Hg = (Hg+ • 22Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 44.4 | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 22Hg) + Hg = (Hg+ • 23Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 46.4 | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 23Hg) + Hg = (Hg+ • 24Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 47.3 | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 10Hg) + Hg = (Hg+ • 11Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 11Hg) + Hg = (Hg+ • 12Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 26. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 12Hg) + Hg = (Hg+ • 13Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 27. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 13Hg) + Hg = (Hg+ • 14Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 28. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 14Hg) + Hg = (Hg+ • 15Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 29. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 15Hg) + Hg = (Hg+ • 16Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 30. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 16Hg) + Hg = (Hg+ • 17Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 33. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 17Hg) + Hg = (Hg+ • 18Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 35. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 18Hg) + Hg = (Hg+ • 19Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 37. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 19Hg) + Hg = (Hg+ • 20Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 41. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 9Hg) + Hg = (Hg+ • 10Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 5Hg) + Hg = (Hg+ • 6Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 6Hg) + Hg = (Hg+ • 7Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 7Hg) + Hg = (Hg+ • 8Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 8Hg) + Hg = (Hg+ • 9Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
By formula: (Hg+ • 4Hg) + Hg = (Hg+ • 5Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 19. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase |
By formula: Hg+ + Hg = (Hg+ • Hg)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 130. | kJ/mol | EI | Haberland, Kornmeier, et al., 1990 | gas phase; from graph |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed 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 |
---|---|---|---|---|
0.092 | Q | N/A | Value at T = 288. K. |
References
Go To: Top, Gas phase thermochemistry data, Condensed 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.
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]
Marsh, 1987
Marsh, K.N.,
Recommended Reference Materials for the Realization of Physicochemical Properties, Blackwell Sci. Pub., Oxford, 1987. [all data]
Honig and Kramer, 1969
Honig, R.E.; Kramer, D.A.,
Vapor pressure data for the solid and liquid elements,
RCA Rev., 1969, 1969, 285. [all data]
Anonymous, 1988
Anonymous, X.,
, NBS Spec. Publ. (U. S.) 260, 1988. [all data]
Timmermans, 1911
Timmermans, J.,
Researches on the freezing point of organic liquid compounds,
Bull. Soc. Chim. Belg., 1911, 25, 300. [all data]
Menzies, 1913
Menzies, A.W.C.,
The Critical Temperature of Mercury,
J. Am. Chem. Soc., 1913, 35, 1065. [all data]
Hicks, 1963
Hicks, W.T.,
Evaluation of Vapor-Pressure Data of Mercury, Lithium, Sodium, and Potassium,
J. Chem. Phys., 1963, 38, 8, 1873-1880, https://doi.org/10.1063/1.1733889
. [all data]
Haberland, Kornmeier, et al., 1990
Haberland, H.; Kornmeier, H.; Langosh, H.; Oschwald, M.; Tanner, G.,
Experimental Study of the Transition from van der Waals, over Covalent to Metallic Bonding in Mercury Clusters,
J. Chem. Soc. Faraday Trans., 1990, 86, 13, 2473, https://doi.org/10.1039/ft9908602473
. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed 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) S°liquid Entropy of liquid at standard conditions 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 ΔfH°gas Enthalpy of formation of gas at standard conditions ΔrH° Enthalpy of reaction at standard conditions - 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.