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This page provides supplementary chemical data on carbon dioxide.
[edit] 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.
[edit] Structure and properties
[edit] Thermodynamic properties
| Phase behavior |
| Triple point |
216.58 K (-56.57 °C), 518.5 kPa |
| Critical point |
304.18 K (31.03 °C), 7.38 MPa |
Std enthalpy change
of fusion, ΔfusHo |
8.647 kJ/mol at triple point[2] |
Std entropy change
of fusion, ΔfusSo |
? J/(mol·K) |
Std enthalpy change
of vaporization,[3] ΔvapHo |
15.326 kJ/mol at –57.5°C |
Std entropy change
of vaporization, ΔvapSo |
70.8 J/(mol·K) |
| Solid properties |
Std enthalpy change
of formation, ΔfHosolid |
? kJ/mol |
Standard molar entropy,
Sosolid |
? J/(mol K) |
| Heat capacity, cp |
? J/(mol K) |
| Liquid properties |
Std enthalpy change
of formation, ΔfHoliquid |
? kJ/mol |
Standard molar entropy,
Soliquid |
? J/(mol K) |
| Heat capacity, cp |
? J/(mol K) |
| Gas properties |
Std enthalpy change
of formation, ΔfHogas |
−393.52 kJ/mol |
Standard molar entropy,
Sogas |
213.79 J/(mol K) |
| Heat capacity,[4] cp |
33.89 J/(mol K) at –75°C
36.33 J/(mol K) at 0°C
36.61 J/(mol K) at 15°C
38.01 J/(mol K) at 100°C
43.81 J/(mol K) at 400°C
50.87 J/(mol K) at 1000°C
56.91 J/(mol K) at 2000°C
53.01 J/(mol K) at 38°C, 2457 kPa
60.01 J/(mol K) at 38°C, 5482 kPa
183.1 J/(mol K) at 38°C, 8653 kPa
|
Heat capacity ratio[4]
γ = cp/cv |
1.37 at –75°C
1.310 at 0°C
1.304 at 15°C
1.281 at 100°C
1.235 at 400°C
1.195 at 1000°C
1.171 at 2000°C
|
| van der Waals' constants[5] |
a = 363.96 L2 kPa/mol2
b = 0.04267 liter per mole |
Equilibrium with carbon monoxide[6]
CO + ½O2 → CO2
K = ![\scriptstyle \frac {[\mathrm {CO_2}]} {[\mathrm {CO}][\mathrm {O_2}]^{\frac {1} {2}}}](http://upload.wikimedia.org/math/1/c/0/1c03086642b0e93f71fa6890252a2504.png)
pK = log10 K
|
pK = 45.0438 at T = 298.16 K
pK = 25.0054 at T = 500 K
pK = 16.5383 at T = 700 K
pK = 11.8409 at T = 900 K
pK = 8.8583 at T = 1100 K
pK = 6.7989 at T = 1300 K
pK = 5.2943 at T = 1500 K
|
[edit] Solubility in water at various temperatures
| Aqueous Solubility of CO2 at 101.3 kPa (1 atm) partial pressure[7] |
| Temperature |
‡Dissolved
CO2 volume
per volume H2O |
grams CO2 per
100 ml H2O |
| 0 °C |
1.713 |
0.3346 |
| 1 °C |
1.646 |
0.3213 |
| 2 °C |
1.527 |
0.3091 |
| 3 °C |
1.527 |
0.2978 |
| 4 °C |
1.473 |
0.2871 |
| 5 °C |
1.424 |
0.2774 |
| 6 °C |
1.377 |
0.2681 |
| 7 °C |
1.331 |
0.2589 |
| 8 °C |
1.282 |
0.2492 |
| 9 °C |
1.237 |
0.2403 |
| 10 °C |
1.194 |
0.2318 |
| 11 °C |
1.154 |
0.2239 |
| 12 °C |
1.117 |
0.2165 |
| 13 °C |
1.083 |
0.2098 |
| 14 °C |
1.050 |
0.2032 |
| 15 °C |
1.019 |
0.1970 |
| 16 °C |
0.985 |
0.1903 |
| 17 °C |
0.956 |
0.1845 |
|
|
| Temperature |
‡Dissolved
CO2 volume
per volume H2O |
grams CO2 per
100 ml H2O |
| 18 °C |
0.928 |
0.1789 |
| 19 °C |
0.902 |
0.1737 |
| 20 °C |
0.878 |
0.1688 |
| 21 °C |
0.854 |
0.1640 |
| 22 °C |
0.829 |
0.1590 |
| 23 °C |
0.804 |
0.1540 |
| 24 °C |
0.781 |
0.1493 |
| 25 °C |
0.759 |
0.1449 |
| 26 °C |
0.738 |
0.1406 |
| 27 °C |
0.718 |
0.1366 |
| 28 °C |
0.699 |
0.1327 |
| 29 °C |
0.682 |
0.1292 |
| 30 °C |
0.655 |
0.1257 |
| 35 °C |
0.592 |
0.1105 |
| 40 °C |
0.530 |
0.0973 |
| 45 °C |
0.479 |
0.0860 |
| 50 °C |
0.436 |
0.0761 |
| 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.
[edit] Vapor pressure of solid and liquid
| P in mm Hg |
1 |
10 |
40 |
100 |
400 |
760 |
1520 |
3800 |
7600 |
15200 |
30400 |
45600 |
| 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 |
60 |
| 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 |
6079.5 |
| 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 |
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.
log of Carbon Dioxide vapor pressure. Uses formula:   obtained from CHERIC [3]
[edit] Phase diagram

[edit] 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 grams/mole. To convert densities to moles/liter, multiply by 22.678 cm3-mole/liter-gram. 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.
| Carbon dioxide liquid/vapor equilibrium thermodynamic data |
Temp.
°C |
Pvap
Vapor
pressure
kPa |
Hliq
Heat
content
liquid
J/g |
Hvap
Heat
content
vapor
J/g |
ΔvapHo
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 |
1081.6 |
|
|
|
|
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 |
42.94 |
| –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 |
3981 |
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 |
|
|
Temp.
°C |
Pvap
Vapor
pressure
kPa |
Hliq
Heat
content
liquid
J/g |
Hvap
Heat
content
vapor
J/g |
ΔvapHo
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 |
[edit] Spectral data
[edit] References
- ^ Lange's Handbook of Chemistry, 10th ed. pp 1669-1674
- ^ "Gas Encyclopaedia". Air Liquide. Retrieved on 1 June 2007.
- ^ a b "Pure Component Properties" (Queriable database). Chemical Engineering Research Information Center. Retrieved on 8 May 2007.
- ^ a b Lange's Handbook of Chemistry, 10th ed, pp 1525-1528
- ^ 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
- Linstrom, P.J.; Mallard, W.G. (eds.) NIST Chemistry WebBook, NIST Standard Reference Database Number 69. National Institute of Standards and Technology, Gaithersburg MD. http://webbook.nist.gov
Except where noted otherwise, data relate to standard ambient temperature and pressure.
Disclaimer applies.
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