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Carbon dioxide (data page)
Chemical data page
Chemical data page
and save the page -- This page provides supplementary chemical data on carbon dioxide.
Material Safety Data Sheet ==
The handling of this chemical may incur notable safety precautions. It is highly recommended that you seek the Material Safety Datasheet (MSDS) for this chemical from a reliable source such as SIRI, and follow its directions. MSDS for solid carbon dioxide is available from Pacific Dry Ice, inc.
Structure and properties ==
| Structure and properties | |
|---|---|
| Index of refraction, *n*D | |
| Dielectric constant, εr | |
| Average energy per C=O bond | |
| Bond length | |
| Bond angle | |
| Magnetic susceptibility | |
| Surface tension | |
| Viscosity of liquid | |
| at equilibrium pressure |
Thermodynamic properties ==
| Phase behavior | Solid properties | Liquid properties | Gas properties | ||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|
| Triple point | 216.58 K, 518.5 kPa | ||||||||||
| Critical point | 304.18 K, 7.38 MPa | ||||||||||
| Std enthalpy change | |||||||||||
| of fusion, Δfus*H*o | url=http://encyclopedia.airliquide.com/encyclopedia.asp?GasID=26 | title=Gas Encyclopaedia | publisher=Air Liquide | accessdate=1 June 2007 | archive-date=23 November 2016 | archive-url=https://web.archive.org/web/20161123090821/http://encyclopedia.airliquide.com/encyclopedia.asp?GasID=26 | url-status=dead}} | ||||
| Entropy change | |||||||||||
| of fusion, Δfus*S* | 40 J/(mol·K) at triple point | ||||||||||
| Std enthalpy change | |||||||||||
| of vaporization, Δvap*H*o | 15.326 kJ/mol at 215.7 K (348 J/g) | ||||||||||
| Std entropy change | |||||||||||
| of vaporization, Δvap*S*o | 70.8 J/(mol·K) | ||||||||||
| Std enthalpy change | |||||||||||
| of formation, Δf*H*osolid | −427.4 kJ/mol | ||||||||||
| doi = 10.1063/1.1749929 | title = Carbon Dioxide. The Heat Capacity and Vapor Pressure of the Solid. The Heat of Sublimation. Thermodynamic and Spectroscopic Values of the Entropy | year = 1937 | last1 = Giauque | first1 = W. F. | last2 = Egan | first2 = C. J. | journal = The Journal of Chemical Physics | volume = 5 | issue = 1 | pages = 45–54 | bibcode = 1937JChPh...5...45G}} |
| *S*osolid | 51.07 J/(mol·K) | ||||||||||
| Heat capacity, *cp* | |||||||||||
| Std enthalpy change | |||||||||||
| of formation, Δf*H*oliquid | −393.5kJ/mol | ||||||||||
| Standard molar entropy, | |||||||||||
| *S*oliquid | 213.7J/(mol K) | ||||||||||
| Heat capacity, *cp* | 80—150 J/(mol·K) at 220—290 K | ||||||||||
| Std enthalpy change | |||||||||||
| of formation, Δf*H*ogas | −393.52 kJ/mol | ||||||||||
| Standard molar entropy, | |||||||||||
| *S*ogas | 213.79 J/(mol·K) | ||||||||||
| title=Ideal Gas Heat Capacity of CARBON DIOXIDE 화학공학소재연구정보센터(CHERIC) 연구정보 KDB Pure Component Properties | url=https://www.cheric.org/research/kdb/hcprop/showcoef.php?prop=CPG | website=www.cheric.org}} *cp* | |||||||||
| Heat capacity ratio | |||||||||||
| *γ* = *cp*/*cv* | |||||||||||
| van der Waals' constants | a = 363.96 L2 kPa/mol2 | ||||||||||
| b = 0.04267 liter per mole | |||||||||||
| Equilibrium with carbon monoxide |
It is used for smoking effects in different scenes.
Solubility in water at various temperatures
| 17 °C | 0.956 | 0.1845 |
|---|
|
| 60 °C | 0.359 | 0.0576 |
|---|
|- |}
- ‡Second column of table indicates solubility at each given temperature in volume of CO2 as it would be measured at 101.3 kPa and 0 °C per volume of water.
- The solubility is given for "pure water", i.e., water which contain only CO2. This water is going to be acidic. For example, at 25 °C the pH of 3.9 is expected (see carbonic acid). At less acidic pH values, the solubility will increase because of the pH-dependent speciation of CO2.
Vapor pressure of solid and liquid
| **T in °C** | −134.3(s) | −119.5(s) | −108.6(s) | −100.2(s) | −85.7(s) | −78.2(s) | −69.1(s) | −56.7 | −39.5 | −18.9 | 5.9 | 22.4 | ||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| **P in mm Hg** | 1 | 10 | 40 | 100 | 400 | 760 | 1520 | 3800 | 7600 | 15200 | 30400 | |||
| **P in atm (2sf, derived from mm Hg)** | 0.0013 | 0.013 | 0.053 | 0.13 | 0.53 | 1.0 | 2.0 | 5.0 | 10 | 20 | 40 | |||
| **P in kPa (derived from mm Hg / atm)** | 0.13 | 1.3 | 5.3 | 13 | 53 | 101.325 | 202.65 | 506.625 | 1013.25 | 2026.5 | 4053 |
Table data obtained from CRC Handbook of Chemistry and Physics 44th ed. Annotation "(s)" indicates equilibrium temperature of vapor over solid. Otherwise temperature is equilibrium of vapor over liquid. For kPa values, where datum is whole numbers of atmospheres exact kPa values are given, elsewhere 2 significant figures derived from mm Hg data.
Phase diagram
Liquid/vapor equilibrium thermodynamic data
The table below gives thermodynamic data of liquid CO2 in equilibrium with its vapor at various temperatures. Heat content data, heat of vaporization, and entropy values are relative to the liquid state at 0 °C temperature and 3483 kPa pressure. To convert heat values to joules per mole values, multiply by 44.095 g/mol. To convert densities to moles per liter, multiply by 22.678 cm3 mol/(L·g). Data obtained from CRC Handbook of Chemistry and Physics, 44th ed. pages 2560–2561, except for critical temperature line (31.1 °C) and temperatures −30 °C and below, which are taken from Lange's Handbook of Chemistry, 10th ed. page 1463.
| Temp. | |||||||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| °C | *Pvap* | ||||||||||||||||
| Vapor | |||||||||||||||||
| pressure | |||||||||||||||||
| kPa | *Hliq* | ||||||||||||||||
| Heat | |||||||||||||||||
| content | |||||||||||||||||
| liquid | |||||||||||||||||
| J/g | *Hvap* | ||||||||||||||||
| Heat | |||||||||||||||||
| content | |||||||||||||||||
| vapor | |||||||||||||||||
| J/g | Δvap*H*o | ||||||||||||||||
| Heat of | |||||||||||||||||
| vapor- | |||||||||||||||||
| ization | |||||||||||||||||
| J/g | *ρvap* | ||||||||||||||||
| Density | |||||||||||||||||
| of vapor | |||||||||||||||||
| g/cm3 | *ρliq* | ||||||||||||||||
| Density | |||||||||||||||||
| of liquid | |||||||||||||||||
| g/cm3 | *Sliq* | ||||||||||||||||
| Entropy | |||||||||||||||||
| liquid | |||||||||||||||||
| J/mol-°C | *Svap* | ||||||||||||||||
| Entropy | |||||||||||||||||
| vapor | |||||||||||||||||
| J/mol-°C | Temp. | ||||||||||||||||
| °C | *Pvap* | ||||||||||||||||
| Vapor | |||||||||||||||||
| pressure | |||||||||||||||||
| kPa | *Hliq* | ||||||||||||||||
| Heat | |||||||||||||||||
| content | |||||||||||||||||
| liquid | |||||||||||||||||
| J/g | *Hvap* | ||||||||||||||||
| Heat | |||||||||||||||||
| content | |||||||||||||||||
| vapor | |||||||||||||||||
| J/g | Δvap*H*o | ||||||||||||||||
| Heat of | |||||||||||||||||
| vapor- | |||||||||||||||||
| ization | |||||||||||||||||
| J/g | *ρvap* | ||||||||||||||||
| Density | |||||||||||||||||
| of vapor | |||||||||||||||||
| g/cm3 | *ρliq* | ||||||||||||||||
| Density | |||||||||||||||||
| of liquid | |||||||||||||||||
| g/cm3 | *Sliq* | ||||||||||||||||
| Entropy | |||||||||||||||||
| liquid | |||||||||||||||||
| J/mol-°C | *Svap* | ||||||||||||||||
| Entropy | |||||||||||||||||
| vapor | |||||||||||||||||
| J/mol-°C | |||||||||||||||||
| −56.6 | 518.3 | 1.179 | |||||||||||||||
| −56.0 | 531.8 | 1.177 | |||||||||||||||
| −54.0 | 579.1 | 1.169 | |||||||||||||||
| −52.0 | 629.6 | 1.162 | |||||||||||||||
| −50.0 | 683.4 | 1.155 | |||||||||||||||
| −48.0 | 740.6 | 1.147 | |||||||||||||||
| −46.0 | 801.3 | 1.139 | |||||||||||||||
| −44.0 | 865.6 | 1.131 | |||||||||||||||
| −42.0 | 933.8 | 1.124 | |||||||||||||||
| −40.0 | 1005.7 | 1.116 | |||||||||||||||
| −38.0 | 1081.9 | 1.108 | |||||||||||||||
| −36.0 | 1161.8 | 1.100 | |||||||||||||||
| −34.0 | 1246.2 | 1.092 | |||||||||||||||
| −32.0 | 1335.1 | 1.084 | |||||||||||||||
| −30.0 | 1428.6 | 1.075 | |||||||||||||||
| −28.89 | 1521 | −55.69 | 237.1 | 292.9 | 0.03846 | 1.0306 | −9.48 | 43.41 | |||||||||
| −27.78 | 1575 | −53.76 | 237.3 | 291.0 | 0.03987 | 1.0276 | −9.13 | 43.21 | |||||||||
| −26.67 | 1630 | −51.84 | 237.6 | 289.4 | 0.04133 | 1.0242 | −8.78 | 43.01 | |||||||||
| −25.56 | 1686 | −49.87 | 237.6 | 287.5 | 0.04283 | 1.0209 | −8.45 | 42.78 | |||||||||
| −24.44 | 1744 | −47.91 | 237.8 | 285.7 | 0.04440 | 1.0170 | −8.10 | 42.56 | |||||||||
| −23.33 | 1804 | −45.94 | 237.8 | 283.6 | 0.04600 | 1.0132 | −7.75 | 42.36 | |||||||||
| −22.22 | 1866 | −43.93 | 237.8 | 281.7 | 0.04767 | 1.0093 | −7.40 | 42.14 | |||||||||
| −21.11 | 1928 | −41.92 | 237.8 | 279.6 | 0.04938 | 1.0053 | −7.05 | 41.94 | |||||||||
| −20.00 | 1993 | −39.91 | 237.8 | 277.8 | 0.05116 | 1.0011 | −6.68 | 41.71 | |||||||||
| −18.89 | 2059 | −37.86 | 237.8 | 275.7 | 0.05300 | 0.9968 | −6.31 | 41.49 | |||||||||
| −17.78 | 2114 | −35.82 | 237.6 | 273.6 | 0.05489 | 0.9923 | −5.98 | 41.27 | |||||||||
| −16.67 | 2197 | −33.73 | 237.6 | 271.2 | 0.05686 | 0.9875 | −5.61 | 41.05 | |||||||||
| −15.56 | 2269 | −31.64 | 237.3 | 269.2 | 0.05888 | 0.9829 | −5.26 | 40.83 | |||||||||
| −14.44 | 2343 | −29.54 | 237.3 | 266.9 | 0.06098 | 0.9782 | −4.91 | 40.61 | |||||||||
| −13.33 | 2418 | −27.41 | 237.1 | 264.5 | 0.06314 | 0.9734 | −4.54 | 40.39 | |||||||||
| −12.22 | 2495 | −25.27 | 236.9 | 262.2 | 0.06539 | 0.9665 | −4.17 | 40.15 | |||||||||
| −11.11 | 2574 | −23.09 | 236.7 | 259.7 | 0.06771 | 0.9639 | −3.80 | 39.92 | |||||||||
| −10.00 | 2654 | −20.90 | 236.4 | 257.3 | 0.07011 | 0.9592 | −3.43 | 39.68 | |||||||||
| −8.89 | 2738 | −18.69 | 235.9 | 254.8 | 0.07259 | 0.9543 | −3.06 | 39.46 | |||||||||
| −7.78 | 2823 | −16.45 | 235.7 | 252.2 | 0.07516 | 0.9494 | −2.69 | 39.22 | |||||||||
| −6.67 | 2910 | −14.18 | 235.2 | 249.4 | 0.07783 | 0.9443 | −2.32 | 38.98 | |||||||||
| −5.56 | 2999 | −11.90 | 234.8 | 246.6 | 0.08059 | 0.9393 | −1.94 | 38.74 | |||||||||
| −4.44 | 3090 | −9.977 | 234.3 | 243.8 | 0.08347 | 0.9340 | −1.57 | 38.50 | |||||||||
| −3.89 | 3136 | −8.410 | 234.1 | 242.4 | 0.08494 | 0.9313 | −1.37 | 38.37 | |||||||||
| −2.78 | 3230 | −6.046 | 233.6 | 239.7 | 0.08797 | 0.9260 | −0.98 | 38.12 | |||||||||
| −1.67 | 3327 | −3.648 | 232.9 | 236.6 | 0.09111 | 0.9206 | −0.59 | 37.88 | |||||||||
| −0.56 | 3425 | −1.222 | 232.4 | 233.6 | 0.09438 | 0.9150 | −0.20 | 37.62 | |||||||||
| 0.56 | 3526 | 1.234 | 231.7 | 230.5 | 0.09776 | 0.9094 | 0.20 | 37.36 | |||||||||
| 1.67 | 3629 | 3.728 | 231.0 | 227.3 | 0.1013 | 0.9036 | 0.61 | 37.08 | |||||||||
| 2.78 | 3735 | 6.268 | 230.4 | 224.0 | 0.1050 | 0.8975 | 1.01 | 36.83 | |||||||||
| 3.89 | 3843 | 8.445 | 229.4 | 220.5 | 0.1088 | 0.8914 | 1.42 | 36.55 | |||||||||
| 5.00 | 3953 | 11.46 | 228.5 | 217.0 | 0.1128 | 0.8850 | 1.83 | 36.25 | |||||||||
| 6.11 | 4067 | 14.13 | 227.6 | 213.4 | 0.1169 | 0.8784 | 2.25 | 35.98 | |||||||||
| 7.22 | 4182 | 16.85 | 226.5 | 209.7 | 0.1213 | 0.8716 | 2.69 | 35.68 | |||||||||
| 8.33 | 4300 | 19.63 | 225.4 | 205.8 | 0.1258 | 0.8645 | 3.12 | 35.39 | |||||||||
| 9.44 | 4420 | 22.46 | 224.3 | 201.8 | 0.1306 | 0.8571 | 3.56 | 35.07 | |||||||||
| 10.56 | 4544 | 25.36 | 223.1 | 197.7 | 0.1355 | 0.8496 | 4.02 | 34.76 | |||||||||
| 11.67 | 4670 | 28.33 | 221.8 | 193.4 | 0.1408 | 0.8418 | 4.48 | 34.45 | |||||||||
| 12.78 | 4798 | 31.35 | 220.3 | 188.9 | 0.1463 | 0.8338 | 4.94 | 34.11 | |||||||||
| 13.89 | 4929 | 34.49 | 218.8 | 184.3 | 0.1521 | 0.8254 | 5.42 | 33.76 | |||||||||
| 15.00 | 5063 | 37.30 | 217.2 | 179.5 | 0.1583 | 0.8168 | 5.92 | 33.41 | |||||||||
| 16.11 | 5200 | 41.03 | 215.1 | 174.4 | 0.1648 | 0.8076 | 6.42 | 33.02 | |||||||||
| 17.22 | 5340 | 44.48 | 213.6 | 169.1 | 0.1717 | 0.7977 | 6.96 | 32.66 | |||||||||
| 18.33 | 5482 | 48.03 | 211.5 | 163.5 | 0.1791 | 0.7871 | 7.49 | 32.25 | |||||||||
| 19.44 | 5628 | 51.71 | 209.4 | 157.6 | 0.1869 | 0.7759 | 8.04 | 31.83 | |||||||||
| 20.56 | 5776 | 55.61 | 207.0 | 151.4 | 0.1956 | 0.7639 | 8.63 | 31.38 | |||||||||
| 21.67 | 5928 | 59.66 | 204.3 | 144.7 | 0.2054 | 0.7508 | 9.24 | 30.90 | |||||||||
| 22.78 | 6083 | 63.97 | 201.5 | 137.5 | 0.2151 | 0.7367 | 9.89 | 30.39 | |||||||||
| 23.89 | 6240 | 68.58 | 198.4 | 129.8 | 0.2263 | 0.7216 | 10.57 | 29.85 | |||||||||
| 25.00 | 6401 | 73.51 | 194.8 | 121.3 | 0.2387 | 0.7058 | 11.31 | 29.24 | |||||||||
| 26.11 | 6565 | 78.91 | 190.7 | 111.8 | 0.2532 | 0.6894 | 12.10 | 28.60 | |||||||||
| 27.22 | 6733 | 84.94 | 186.0 | 101.1 | 0.2707 | 0.6720 | 12.99 | 27.84 | |||||||||
| 28.33 | 6902 | 91.88 | 180.4 | 88.49 | 0.2923 | 0.6507 | 14.00 | 26.95 | |||||||||
| 29.44 | 7081 | 100.4 | 173.1 | 72.72 | 0.3204 | 0.6209 | 15.24 | 25.85 | |||||||||
| 30.00 | 7164 | 105.6 | 168.4 | 62.76 | 0.3378 | 0.5992 | 16.01 | 25.15 | |||||||||
| 30.56 | 7253 | 112.3 | 162.3 | 50.04 | 0.3581 | 0.5661 | 16.99 | 24.24 | |||||||||
| 31.1 | 7391 | 0.00 | 0.4641 | 0.4641 |
Spectral data ==
| UV-Vis | IR | NMR | MS | ||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| λmax | ? nm | ||||||||||||||
| Extinction coefficient, ε | ? | ||||||||||||||
| last1=Martin | first1=P. E. | last2=Barker | first2=E. F. | title=The Infrared Absorption Spectrum of Carbon Dioxide | journal=Physical Review | volume=41 | issue=3 | year=1932 | pages=291–303 | issn=0031-899X | doi=10.1103/PhysRev.41.291 | bibcode=1932PhRv...41..291M}} | 2347 and 667 cm−1 | ||
| Proton NMR | not applicable | ||||||||||||||
| Carbon-13 NMR | last1=Reich | first1=H. J. | title=C-13 Chemical Shifts | url=http://www.chem.wisc.edu/areas/reich/handouts/nmr-c13/cdata.htm | website=Organic Chem Info | publisher=University of Wisconsin | accessdate=31 May 2015 | ref=reich13Cnmr | archive-url=https://web.archive.org/web/20150302024127/http://www.chem.wisc.edu/areas/reich/handouts/nmr-c13/cdata.htm | archive-date=2 March 2015 | url-status=dead}} | ||||
| Masses of main fragments |
Notes
References
References
- "Refractive index of gases". NPL.
- Darwent, B. deB. (1970). "Bond Dissociation Energies in Simple Molecules" Nat. Stand. Ref. Data Ser., Nat. Bur. Stand. (U.S.) 31, 52 pages.
- "CCCBDB listing of experimental data page 2".
- Anderson, Kelly E.. (2009-03-12). "Bond Angle Distributions of Carbon Dioxide in the Gas, Supercritical, and Solid Phases". The Journal of Physical Chemistry A.
- ''Lange's Handbook of Chemistry'', 10th ed. pp. 1669–1674
- "Gas Encyclopaedia". Air Liquide.
- "Carbon dioxide 화학공학소재연구정보센터(CHERIC) {{!}} 연구정보 {{!}} KDB {{!}} Pure Component Properties".
- (1937). "Carbon Dioxide. The Heat Capacity and Vapor Pressure of the Solid. The Heat of Sublimation. Thermodynamic and Spectroscopic Values of the Entropy". The Journal of Chemical Physics.
- "Liquid Heat Capcity of CARBON DIOXIDE 화학공학소재연구정보센터(CHERIC) {{!}} 연구정보 {{!}} KDB {{!}} Pure Component Properties".
- ''Lange's Handbook of Chemistry'', 10th ed, pp. 1525–1528.
- "Ideal Gas Heat Capacity of CARBON DIOXIDE 화학공학소재연구정보센터(CHERIC) {{!}} 연구정보 {{!}} KDB {{!}} Pure Component Properties".
- ''Lange's Handbook of Chemistry'', 10th ed, pp. 1522–1524.
- ''Lange's Handbook of Chemistry'', 10th ed. pp. 1573–1576.
- ''Lange's Handbook of Chemistry'', 10th ed., p. 1100
- "Pure Component Properties". Chemical Engineering Research Information Center.
- (1932). "The Infrared Absorption Spectrum of Carbon Dioxide". Physical Review.
- (2019). "Carbon dioxide absorption spectroscopy with a mid-infrared silicon photonic waveguide". Optics Letters.
- Reichle, Henry G.. (May 1969). "The Effect of Several Infrared Transparent Broadening Gases on the Absorption of Infrared Radiation in the 15 μm Band of Carbon Dioxide". High Altitude Engineering Laboratory.
- "C-13 Chemical Shifts". University of Wisconsin.
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