Dortmund Data Bank
Excess Volume Data
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.
Excess Volume Data Set 1046
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
Excess Volume [cm3/mol] |
x1 [mol/mol] |
-0.0082 |
0.00150 |
-0.0161 |
0.00290 |
-0.0396 |
0.00710 |
-0.0664 |
0.01150 |
-0.1321 |
0.02060 |
-0.1829 |
0.02730 |
-0.2416 |
0.03500 |
-0.2789 |
0.03990 |
-0.2875 |
0.04100 |
-0.3825 |
0.05420 |
-0.4857 |
0.06690 |
-0.5755 |
0.08030 |
-0.5902 |
0.08410 |
-0.6634 |
0.09960 |
-0.7234 |
0.11380 |
-0.8379 |
0.16300 |
-0.8936 |
0.19540 |
-0.9508 |
0.24680 |
-0.9842 |
0.30290 |
-0.9911 |
0.33870 |
-0.9925 |
0.39060 |
-0.9818 |
0.42630 |
-0.9637 |
0.46130 |
-0.9113 |
0.53510 |
-0.8819 |
0.56610 |
-0.8286 |
0.61370 |
-0.7521 |
0.66950 |
-0.6774 |
0.71940 |
-0.6210 |
0.75460 |
-0.5287 |
0.80120 |
-0.4384 |
0.84480 |
-0.3510 |
0.87990 |
-0.2806 |
0.91010 |
-0.1730 |
0.95080 |
-0.1190 |
0.96430 |
-0.0669 |
0.98080 |
Reference
Source |
Davis M.I.; Ham E.S.: Part 2. Comparisons of the propanol isomers in their aqueous mixtures. Thermochim.Acta 190 (1991) 251-258 |
Excess Volume Data Set 1915
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
Excess Volume [cm3/mol] |
x1 [mol/mol] |
-0.06291 |
0.01000 |
-0.13094 |
0.02000 |
-0.2063 |
0.03000 |
-0.2819 |
0.04000 |
-0.35574 |
0.05000 |
-0.42496 |
0.06000 |
-0.4858 |
0.07000 |
-0.5394 |
0.08000 |
-0.5854 |
0.09000 |
-0.6260 |
0.10000 |
-0.6614 |
0.11000 |
-0.6921 |
0.12000 |
-0.7180 |
0.13000 |
-0.7416 |
0.14000 |
-0.7646 |
0.15000 |
-0.7860 |
0.16000 |
-0.8040 |
0.17000 |
-0.8199 |
0.18000 |
-0.8354 |
0.19000 |
-0.8496 |
0.20000 |
-0.8620 |
0.21000 |
-0.8733 |
0.22000 |
-0.8852 |
0.23000 |
-0.8963 |
0.24000 |
-0.9052 |
0.25000 |
-0.9135 |
0.26000 |
-0.9199 |
0.27000 |
-0.9257 |
0.28000 |
-0.9299 |
0.29000 |
-0.9338 |
0.30000 |
-0.9363 |
0.31000 |
-0.9384 |
0.32000 |
-0.9393 |
0.33000 |
-0.9406 |
0.34000 |
-0.9423 |
0.35000 |
-0.9439 |
0.36000 |
-0.9444 |
0.37000 |
-0.9436 |
0.38000 |
-0.9415 |
0.39000 |
-0.9382 |
0.40000 |
-0.9333 |
0.41000 |
-0.9292 |
0.42000 |
-0.9258 |
0.43000 |
-0.9226 |
0.44000 |
-0.9193 |
0.45000 |
-0.9153 |
0.46000 |
-0.9109 |
0.47000 |
-0.9055 |
0.48000 |
-0.8991 |
0.49000 |
-0.8925 |
0.50000 |
-0.8851 |
0.51000 |
-0.8769 |
0.52000 |
-0.8681 |
0.53000 |
-0.8588 |
0.54000 |
-0.8488 |
0.55000 |
-0.8385 |
0.56000 |
-0.8277 |
0.57000 |
-0.8165 |
0.58000 |
-0.8051 |
0.59000 |
-0.7935 |
0.60000 |
-0.7818 |
0.61000 |
-0.7693 |
0.62000 |
-0.7561 |
0.63000 |
-0.7422 |
0.64000 |
-0.7284 |
0.65000 |
-0.7140 |
0.66000 |
-0.6992 |
0.67000 |
-0.6838 |
0.68000 |
-0.6688 |
0.69000 |
-0.6541 |
0.70000 |
-0.6399 |
0.71000 |
-0.6246 |
0.72000 |
-0.6092 |
0.73000 |
-0.5936 |
0.74000 |
-0.5770 |
0.75000 |
-0.5596 |
0.76000 |
-0.5413 |
0.77000 |
-0.5230 |
0.78000 |
-0.5046 |
0.79000 |
-0.4855 |
0.80000 |
-0.4656 |
0.81000 |
-0.44504 |
0.82000 |
-0.4237 |
0.83000 |
-0.4034 |
0.84000 |
-0.38164 |
0.85000 |
-0.3601 |
0.86000 |
-0.33884 |
0.87000 |
-0.31703 |
0.88000 |
-0.2947 |
0.89000 |
-0.27183 |
0.90000 |
-0.24757 |
0.91000 |
-0.2219 |
0.92000 |
-0.19478 |
0.93000 |
-0.1672 |
0.94000 |
-0.1401 |
0.95000 |
-0.11067 |
0.96000 |
-0.07983 |
0.97000 |
-0.05056 |
0.98000 |
-0.022896 |
0.99000 |
Reference
Source |
Langdon W.M.; Keyes D.B.: Isopropyl Alcohol-Water System.. Ind.Eng.Chem. 35 (1943) 459-464 |
Excess Volume Data Set 4458
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
Excess Volume [cm3/mol] |
x1 [mol/mol] |
-0.027857 |
0.004091 |
-0.15652 |
0.02220 |
-0.2591 |
0.03790 |
-0.3158 |
0.04712 |
-0.6481 |
0.11411 |
-0.7564 |
0.14401 |
-0.8618 |
0.18152 |
-0.9795 |
0.42759 |
-0.8950 |
0.53562 |
-0.8584 |
0.57104 |
-0.5909 |
0.79341 |
-0.5066 |
0.84164 |
-0.3121 |
0.92152 |
-0.12147 |
0.97452 |
Reference
Source |
Yamamoto H.; Ichikawa K.; Tokunaga J.: Solubility of Helium in Methanol + Water, Ethanol + Water, 1-Propanol + Water, and 2-Propanol + Water Solutions at 25 °C. J.Chem.Eng.Data 39 (1994) 155-157 |
Diagrams
List of All References
Source |
Davis M.I.; Ham E.S.: Part 2. Comparisons of the propanol isomers in their aqueous mixtures. Thermochim.Acta 190 (1991) 251-258 |
Langdon W.M.; Keyes D.B.: Isopropyl Alcohol-Water System.. Ind.Eng.Chem. 35 (1943) 459-464 |
Yamamoto H.; Ichikawa K.; Tokunaga J.: Solubility of Helium in Methanol + Water, Ethanol + Water, 1-Propanol + Water, and 2-Propanol + Water Solutions at 25 °C. J.Chem.Eng.Data 39 (1994) 155-157 |
Excess Volume Data Overview
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