Dortmund Data Bank
G-function (G-G0)/T of Water
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Component
| Formula |
Molar Mass |
CAS Registry Number |
Name |
| H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of Water
Diagrams
Data Table
| T [K] |
G-function (G-G0)/T [J/(mol*K)] |
State |
Reference |
| 50.00 |
-96.71 |
Vapor |
3 |
| 60.00 |
-102.64 |
Vapor |
3 |
| 70.00 |
-107.68 |
Vapor |
3 |
| 80.00 |
-112.05 |
Vapor |
3 |
| 90.00 |
-115.92 |
Vapor |
3 |
| 100.00 |
-119.38 |
Vapor |
2 |
| 110.00 |
-122.52 |
Vapor |
3 |
| 120.00 |
-125.38 |
Vapor |
3 |
| 130.00 |
-128.02 |
Vapor |
3 |
| 140.00 |
-130.47 |
Vapor |
3 |
| 150.00 |
-132.75 |
Vapor |
3 |
| 160.00 |
-134.88 |
Vapor |
3 |
| 170.00 |
-136.88 |
Vapor |
3 |
| 180.00 |
-138.77 |
Vapor |
3 |
| 190.00 |
-140.56 |
Vapor |
3 |
| 200.00 |
-142.26 |
Vapor |
2 |
| 210.00 |
-143.87 |
Vapor |
3 |
| 220.00 |
-145.41 |
Vapor |
3 |
| 230.00 |
-146.89 |
Vapor |
3 |
| 240.00 |
-148.30 |
Vapor |
3 |
| 250.00 |
-149.65 |
Vapor |
3 |
| 260.00 |
-150.95 |
Vapor |
3 |
| 270.00 |
-152.22 |
Vapor |
3 |
| 273.15 |
-152.59 |
Vapor |
2 |
| 280.00 |
-153.41 |
Vapor |
3 |
| 290.00 |
-154.58 |
Vapor |
3 |
| 298.15 |
-155.56 |
Vapor |
4 |
| 298.15 |
-155.49 |
Vapor |
2 |
| 298.16 |
-155.54 |
Vapor |
1 |
| 300.00 |
-155.77 |
Vapor |
4 |
| 300.00 |
-155.75 |
Vapor |
1 |
| 300.00 |
-155.70 |
Vapor |
2 |
| 310.00 |
-156.79 |
Vapor |
3 |
| 320.00 |
-157.85 |
Vapor |
3 |
| 330.00 |
-158.87 |
Vapor |
3 |
| 340.00 |
-159.86 |
Vapor |
3 |
| 350.00 |
-160.88 |
Vapor |
4 |
| 350.00 |
-160.83 |
Vapor |
3 |
| 360.00 |
-161.76 |
Vapor |
3 |
| 370.00 |
-162.68 |
Vapor |
3 |
| 380.00 |
-163.57 |
Vapor |
3 |
| 390.00 |
-164.43 |
Vapor |
3 |
| 400.00 |
-165.32 |
Vapor |
1 |
| 400.00 |
-165.28 |
Vapor |
2 |
| 450.00 |
-169.25 |
Vapor |
4 |
| 450.00 |
-169.21 |
Vapor |
3 |
| 500.00 |
-172.80 |
Vapor |
1 |
| 500.00 |
-172.78 |
Vapor |
4 |
| 500.00 |
-172.75 |
Vapor |
2 |
| 550.00 |
-175.99 |
Vapor |
4 |
| 550.00 |
-175.97 |
Vapor |
3 |
| 600.00 |
-178.96 |
Vapor |
1 |
| 600.00 |
-178.93 |
Vapor |
4 |
| 600.00 |
-178.92 |
Vapor |
2 |
| 650.00 |
-181.65 |
Vapor |
3 |
| 700.00 |
-184.23 |
Vapor |
1 |
| 700.00 |
-184.19 |
Vapor |
2 |
| 700.00 |
-184.18 |
Vapor |
4 |
| 750.00 |
-186.57 |
Vapor |
3 |
| 750.00 |
-186.55 |
Vapor |
4 |
| 800.00 |
-188.85 |
Vapor |
1 |
| 800.00 |
-188.81 |
Vapor |
2 |
| 800.00 |
-188.79 |
Vapor |
4 |
| 850.00 |
-190.93 |
Vapor |
3 |
| 850.00 |
-190.90 |
Vapor |
4 |
| 900.00 |
-193.00 |
Vapor |
1 |
| 900.00 |
-192.95 |
Vapor |
2 |
| 900.00 |
-192.91 |
Vapor |
4 |
| 950.00 |
-194.86 |
Vapor |
3 |
| 950.00 |
-194.82 |
Vapor |
4 |
| 1000.00 |
-196.74 |
Vapor |
1 |
| 1000.00 |
-196.70 |
Vapor |
2 |
| 1000.00 |
-196.64 |
Vapor |
4 |
| 1050.00 |
-198.45 |
Vapor |
3 |
| 1050.00 |
-198.40 |
Vapor |
4 |
| 1100.00 |
-200.20 |
Vapor |
1 |
| 1100.00 |
-200.15 |
Vapor |
2 |
| 1100.00 |
-200.08 |
Vapor |
4 |
| 1150.00 |
-201.69 |
Vapor |
4 |
| 1150.00 |
-200.14 |
Vapor |
3 |
| 1200.00 |
-203.39 |
Vapor |
1 |
| 1200.00 |
-203.34 |
Vapor |
2 |
| 1200.00 |
-203.26 |
Vapor |
4 |
| 1200.00 |
-201.77 |
Vapor |
3 |
| 1250.00 |
-204.77 |
Vapor |
4 |
| 1250.00 |
-203.34 |
Vapor |
3 |
| 1300.00 |
-206.38 |
Vapor |
1 |
| 1300.00 |
-206.32 |
Vapor |
2 |
| 1300.00 |
-206.23 |
Vapor |
4 |
| 1400.00 |
-209.19 |
Vapor |
1 |
| 1400.00 |
-209.13 |
Vapor |
2 |
| 1400.00 |
-209.12 |
Vapor |
3 |
| 1400.00 |
-209.02 |
Vapor |
4 |
| 1500.00 |
-211.84 |
Vapor |
1 |
| 1500.00 |
-211.78 |
Vapor |
2 |
| 1500.00 |
-211.77 |
Vapor |
3 |
| 1500.00 |
-211.65 |
Vapor |
4 |
| 1600.00 |
-214.29 |
Vapor |
2 |
| 1600.00 |
-214.28 |
Vapor |
3 |
| 1700.00 |
-216.69 |
Vapor |
2 |
| 1700.00 |
-216.67 |
Vapor |
3 |
| 1800.00 |
-218.98 |
Vapor |
2 |
| 1800.00 |
-218.96 |
Vapor |
3 |
| 1900.00 |
-221.17 |
Vapor |
2 |
| 1900.00 |
-221.15 |
Vapor |
3 |
| 2000.00 |
-223.28 |
Vapor |
2 |
| 2000.00 |
-223.26 |
Vapor |
3 |
| 2100.00 |
-225.28 |
Vapor |
3 |
| 2200.00 |
-227.26 |
Vapor |
2 |
| 2200.00 |
-227.24 |
Vapor |
3 |
| 2300.00 |
-229.13 |
Vapor |
3 |
| 2400.00 |
-230.98 |
Vapor |
2 |
| 2400.00 |
-230.95 |
Vapor |
3 |
| 2500.00 |
-232.72 |
Vapor |
3 |
| 2600.00 |
-234.48 |
Vapor |
2 |
| 2600.00 |
-234.44 |
Vapor |
3 |
| 2700.00 |
-236.10 |
Vapor |
3 |
| 2800.00 |
-237.77 |
Vapor |
2 |
| 2800.00 |
-237.72 |
Vapor |
3 |
| 2900.00 |
-239.30 |
Vapor |
3 |
| 3000.00 |
-240.89 |
Vapor |
2 |
| 3000.00 |
-240.83 |
Vapor |
3 |
| 3200.00 |
-243.85 |
Vapor |
2 |
| 3200.00 |
-243.78 |
Vapor |
3 |
| 3400.00 |
-246.68 |
Vapor |
2 |
| 3400.00 |
-246.60 |
Vapor |
3 |
| 3600.00 |
-249.38 |
Vapor |
2 |
| 3600.00 |
-249.28 |
Vapor |
3 |
| 3800.00 |
-251.96 |
Vapor |
2 |
| 3800.00 |
-251.85 |
Vapor |
3 |
| 4000.00 |
-254.44 |
Vapor |
2 |
| 4000.00 |
-254.31 |
Vapor |
3 |
| 4200.00 |
-256.83 |
Vapor |
2 |
| 4200.00 |
-256.68 |
Vapor |
3 |
| 4400.00 |
-259.12 |
Vapor |
2 |
| 4400.00 |
-258.96 |
Vapor |
3 |
| 4600.00 |
-261.34 |
Vapor |
2 |
| 4600.00 |
-261.16 |
Vapor |
3 |
| 4800.00 |
-263.48 |
Vapor |
2 |
| 4800.00 |
-263.28 |
Vapor |
3 |
| 5000.00 |
-265.55 |
Vapor |
2 |
| 5000.00 |
-265.33 |
Vapor |
3 |
| 5200.00 |
-267.55 |
Vapor |
2 |
| 5400.00 |
-269.50 |
Vapor |
2 |
| 5600.00 |
-271.39 |
Vapor |
2 |
| 5800.00 |
-273.22 |
Vapor |
2 |
| 6000.00 |
-275.00 |
Vapor |
2 |
List of References
| Number |
Source |
| 1 |
Brickwedde F.G.; Moskow M.; Aston J.G.: Equilibrium Constants of some Reactions Involved in the Production Of1,3-Butadiene.. J.Res. NBS 37 (1946) 263-279 |
| 2 |
McBride B.J.; Gordon S.: Thermodynamic functions of several triatomic molecules in the ideal gas state.. J.Chem.Phys. 35 (1961) 2198-2206 |
| 3 |
Friedman A.S.; Haar L.: High-speed machine computation of ideal gas thermodynamic functions.I. Isotopic water molecules.. J.Chem.Phys. 22 (1954) 2051-2058 |
| 4 |
Gordon A.R.: Calculation of thermodynamic quantities from spectroscopic data for polyatomic molecules; the free energy, entropy and heat capacity of steam.. J.Chem.Phys. 2 (1934) 65-72 |
Pure Component Data Overview
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