Carbon dioxide
- Formula: CO2
- Molecular weight: 44.0095
- IUPAC Standard InChIKey: CURLTUGMZLYLDI-UHFFFAOYSA-N
- CAS Registry Number: 124-38-9
- 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. - Isotopologues:
- Other names: Carbon oxide (CO2); Carbonic acid, gas; Carbonic anhydride; Dry ice; CO2; Anhydride carbonique; Carbonica; Kohlendioxyd; Kohlensaure; UN 1013; UN 1845; UN 2187; Cardice; Dricold; Drikold; Carbonic acid anhydride; Khladon 744; R 744
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Phase change data
Go To: Top, 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 |
---|---|---|---|---|---|
Ttriple | 216.58 | K | N/A | Marsh, 1987 | Uncertainty assigned by TRC = 0.008 K; recommended as fixed point for thermometery; TRC |
Ttriple | 216.58 | K | N/A | Angus, Armstrong, et al., 1976 | Uncertainty assigned by TRC = 0.03 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 5.185 | bar | N/A | Angus, Armstrong, et al., 1976 | Uncertainty assigned by TRC = 0.005 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 304.18 | K | N/A | Suehiro, Nakajima, et al., 1996 | Uncertainty assigned by TRC = 0.04 K; TRC |
Tc | 304.1 | K | N/A | Weber, 1989 | Uncertainty assigned by TRC = 0.1 K; TRC |
Tc | 304.35 | K | N/A | Li and Kiran, 1988 | Uncertainty assigned by TRC = 0.4 K; TRC |
Tc | 304.200 | K | N/A | Morrison, 1981 | Uncertainty assigned by TRC = 0.02 K; TRC |
Tc | 304.23 | K | N/A | Efremova and Shvarts, 1972 | Visual, agreement with literature evidence of sample purity; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 73.80 | bar | N/A | Suehiro, Nakajima, et al., 1996 | Uncertainty assigned by TRC = 0.15 bar; TRC |
Pc | 73.40 | bar | N/A | Li and Kiran, 1988 | Uncertainty assigned by TRC = 0.50 bar; TRC |
Pc | 73.825 | bar | N/A | Angus, Armstrong, et al., 1976 | Uncertainty assigned by TRC = 0.005 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.0919 | l/mol | N/A | Li and Kiran, 1988 | Uncertainty assigned by TRC = 0.001 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 10.6 | mol/l | N/A | Suehiro, Nakajima, et al., 1996 | Uncertainty assigned by TRC = 0.05 mol/l; TRC |
ρc | 10.590 | mol/l | N/A | Angus, Armstrong, et al., 1976 | Uncertainty assigned by TRC = 0.007 mol/l; TRC |
ρc | 10.8 | mol/l | N/A | Andrizhievskii and Chernova, 1970 | Uncertainty assigned by TRC = 0.2 mol/l; TRC |
ρc | 10.64 | mol/l | N/A | Lowry and Erickson, 1927 | Uncertainty assigned by TRC = 0.034 mol/l; from a plot of (DN(liq) + DN(g))/2 based on exp. measurement and extrapolated to 31.0 deg C; TRC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
16.7 | 288. | A | Stephenson and Malanowski, 1987 | Based on data from 273. to 304. K.; AC |
16.4 | 258. | A | Stephenson and Malanowski, 1987 | Based on data from 216. to 273. K.; AC |
16.5 | 282. | N/A | Boublík and Aim, 1972 | Based on data from 267. to 303. K.; 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 |
---|---|---|---|---|---|
154.26 to 195.89 | 6.81228 | 1301.679 | -3.494 | Giauque and Egan, 1937 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
26.1 | 207. | A | Stephenson and Malanowski, 1987 | Based on data from 198. to 216. K.; AC |
27.2 ± 0.4 | 70. to 102. | LE | Bryson, Cazcarra, et al., 1974 | AC |
25.9 | 188. | N/A | Ambrose, 1956 | Based on data from 179. to 198. K.; AC |
26.3 | 167. | A | Stull, 1947 | Based on data from 139. to 195. K.; AC |
25.2 | 195. | N/A | Giauque and Egan, 1937, 2 | Based on data from 154. to 196. K.; AC |
References
Go To: Top, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Marsh, 1987
Marsh, K.N.,
Recommended Reference Materials for the Realization of Physicochemical Properties, Blackwell Sci. Pub., Oxford, 1987. [all data]
Angus, Armstrong, et al., 1976
Angus, S.; Armstrong, B.; de Reuck, K.M.,
International Thermodynamic Tables of the Fluid State - 3 Carbon Dioxide, Pergamon, New York, 1976. [all data]
Suehiro, Nakajima, et al., 1996
Suehiro, Y.; Nakajima, M.; Yamada, K.; Uematsu, M.,
Critical parameters of {xCO2 + (1 - x)CHF3} for x = (1.0000, 0.7496, 0.5013 , and 0.2522),
J. Chem. Thermodyn., 1996, 28, 1153-1164. [all data]
Weber, 1989
Weber, L.A.,
Simple Apparatus for Vapor-Liquid Equilibrium Measurements with Data for the Binary Systems of Carbon Dioxide with n-Butane and Isobutane,
J. Chem. Eng. Data, 1989, 34, 171. [all data]
Li and Kiran, 1988
Li, L.; Kiran, E.,
Gas-Liquid Critical Properties of Methylamine + Nitrous Oxide and Methylamine + Ethylene Binary Mixtures,
J. Chem. Eng. Data, 1988, 33, 342. [all data]
Morrison, 1981
Morrison, G.,
Effect of water on the critical points of carbon dioxide and ethane,
J. Phys. Chem., 1981, 85, 759-61. [all data]
Efremova and Shvarts, 1972
Efremova, G.D.; Shvarts, A.V.,
Higher-order Critical Phenomena in Ternary Systems. The Methanol-Carbon Dioxide-Ethane System,
Russ. J. Phys. Chem. (Engl. Transl.), 1972, 46, 237-239. [all data]
Andrizhievskii and Chernova, 1970
Andrizhievskii, A.A.; Chernova, N.I.,
Application of the Moving Meniscus Method in the Study of the Critical Phenomena in One-component Systems,
Russ. J. Phys. Chem. (Engl. Transl.), 1970, 44, 1519. [all data]
Lowry and Erickson, 1927
Lowry, H.H.; Erickson, W.R.,
The Densities of Coexisting Liquid and Gaseous Carbon Dioxide and the Solubility of Water in Liquid Carbon Dioxide.,
J. Am. Chem. Soc., 1927, 49, 2729-2734. [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]
Boublík and Aim, 1972
Boublík, T.; Aim, K.,
Heats of vaporization of simple non-spherical molecule compounds,
Collect. Czech. Chem. Commun., 1972, 37, 11, 3513-3521, https://doi.org/10.1135/cccc19723513
. [all data]
Giauque and Egan, 1937
Giauque, W.F.; Egan, C.J.,
Carbon Dioxide. The Heat Capacity and Vapor Pressure of the Solid. The Heat of Sublimation. Thermodynamic and Spectroscopic Values of the Entropy,
J. Chem. Phys., 1937, 5, 1, 45-54, https://doi.org/10.1063/1.1749929
. [all data]
Bryson, Cazcarra, et al., 1974
Bryson, Charles E.; Cazcarra, Victor; Levenson, Leonard L.,
Sublimation rates and vapor pressures of water, carbon dioxide, nitrous oxide, and xenon,
J. Chem. Eng. Data, 1974, 19, 2, 107-110, https://doi.org/10.1021/je60061a021
. [all data]
Ambrose, 1956
Ambrose, D.,
The vapour pressures and critical temperatures of acetylene and carbon dioxide,
Trans. Faraday Soc., 1956, 52, 772, https://doi.org/10.1039/tf9565200772
. [all data]
Stull, 1947
Stull, Daniel R.,
Vapor Pressure of Pure Substances. Organic and Inorganic Compounds,
Ind. Eng. Chem., 1947, 39, 4, 517-540, https://doi.org/10.1021/ie50448a022
. [all data]
Giauque and Egan, 1937, 2
Giauque, W.F.; Egan, C.J.,
Carbon Dioxide. The Heat Capacity and Vapor Pressure of the Solid. The Heat of Sublimation. Thermodynamic and Spectroscopic Values of the Entropy,
J. Chem. Phys., 1937, 5, 1, 45, https://doi.org/10.1063/1.1749929
. [all data]
Notes
Go To: Top, Phase change data, References
- Symbols used in this document:
Pc Critical pressure Ptriple Triple point pressure Tc Critical temperature Ttriple Triple point temperature Vc Critical volume ΔsubH Enthalpy of sublimation ΔvapH Enthalpy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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