Mixture of 1-Propanol + N,N-Dimethylaminoethanol
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of N,N-Dimethylaminoethanol (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.20 |
100.00 |
0.2007 |
-0.1914 |
298.20 |
100.00 |
0.2509 |
-0.2138 |
298.20 |
100.00 |
0.3008 |
-0.2309 |
298.20 |
100.00 |
0.3505 |
-0.2438 |
298.20 |
100.00 |
0.3999 |
-0.2508 |
298.20 |
100.00 |
0.4507 |
-0.2519 |
298.20 |
100.00 |
0.4990 |
-0.2537 |
298.20 |
100.00 |
0.5509 |
-0.2450 |
298.20 |
100.00 |
0.6000 |
-0.2344 |
298.20 |
100.00 |
0.6505 |
-0.2193 |
298.20 |
10000.00 |
0.2001 |
-0.1911 |
298.20 |
10000.00 |
0.2503 |
-0.2139 |
298.20 |
10000.00 |
0.3004 |
-0.2312 |
298.20 |
10000.00 |
0.3502 |
-0.2434 |
298.20 |
10000.00 |
0.3995 |
-0.2517 |
298.20 |
10000.00 |
0.4504 |
-0.2547 |
298.20 |
10000.00 |
0.5007 |
-0.2530 |
298.20 |
10000.00 |
0.5504 |
-0.2454 |
298.20 |
10000.00 |
0.5994 |
-0.2344 |
298.20 |
10000.00 |
0.6497 |
-0.2205 |
313.20 |
100.00 |
0.2984 |
-0.2512 |
313.20 |
100.00 |
0.3505 |
-0.2669 |
313.20 |
100.00 |
0.4012 |
-0.2762 |
313.20 |
100.00 |
0.4501 |
-0.2794 |
313.20 |
100.00 |
0.5004 |
-0.2771 |
313.20 |
100.00 |
0.5488 |
-0.2686 |
313.20 |
100.00 |
0.5985 |
-0.2565 |
313.20 |
100.00 |
0.6497 |
-0.2389 |
313.20 |
100.00 |
0.6986 |
-0.2167 |
313.20 |
100.00 |
0.7488 |
-0.1904 |
313.20 |
100.00 |
0.8005 |
-0.1578 |
313.20 |
100.00 |
0.8495 |
-0.1244 |
313.20 |
10000.00 |
0.2492 |
-0.2313 |
313.20 |
10000.00 |
0.2998 |
-0.2555 |
313.20 |
10000.00 |
0.3489 |
-0.2701 |
313.20 |
10000.00 |
0.3995 |
-0.2792 |
313.20 |
10000.00 |
0.4484 |
-0.2820 |
313.20 |
10000.00 |
0.4986 |
-0.2802 |
313.20 |
10000.00 |
0.5504 |
-0.2718 |
313.20 |
10000.00 |
0.6001 |
-0.2584 |
313.20 |
10000.00 |
0.6512 |
-0.2396 |
313.20 |
10000.00 |
0.7000 |
-0.2166 |
313.20 |
10000.00 |
0.7501 |
-0.1894 |
313.20 |
10000.00 |
0.8015 |
-0.1567 |
313.20 |
10000.00 |
0.8503 |
-0.1228 |
328.20 |
100.00 |
0.2007 |
-0.2644 |
328.20 |
100.00 |
0.2509 |
-0.2912 |
328.20 |
100.00 |
0.3008 |
-0.3129 |
328.20 |
100.00 |
0.3505 |
-0.3269 |
328.20 |
100.00 |
0.3999 |
-0.3330 |
328.20 |
100.00 |
0.4507 |
-0.3333 |
328.20 |
100.00 |
0.4990 |
-0.3269 |
328.20 |
100.00 |
0.5509 |
-0.3133 |
328.20 |
100.00 |
0.6000 |
-0.2957 |
328.20 |
100.00 |
0.6505 |
-0.2721 |
328.20 |
100.00 |
0.7001 |
-0.2448 |
328.20 |
10000.00 |
0.2001 |
-0.2636 |
328.20 |
10000.00 |
0.2503 |
-0.2932 |
328.20 |
10000.00 |
0.3004 |
-0.3167 |
328.20 |
10000.00 |
0.3502 |
-0.3306 |
328.20 |
10000.00 |
0.3995 |
-0.3382 |
328.20 |
10000.00 |
0.4504 |
-0.3393 |
328.20 |
10000.00 |
0.5007 |
-0.3318 |
328.20 |
10000.00 |
0.5504 |
-0.3195 |
328.20 |
10000.00 |
0.5994 |
-0.3022 |
328.20 |
10000.00 |
0.6497 |
-0.2792 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of N,N-Dimethylaminoethanol (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.20 |
100.00 |
0.2007 |
-0.1914 |
298.20 |
100.00 |
0.2509 |
-0.2138 |
298.20 |
100.00 |
0.3008 |
-0.2309 |
298.20 |
100.00 |
0.3505 |
-0.2438 |
298.20 |
100.00 |
0.3999 |
-0.2508 |
298.20 |
100.00 |
0.4507 |
-0.2519 |
298.20 |
100.00 |
0.4990 |
-0.2537 |
298.20 |
100.00 |
0.5509 |
-0.2450 |
298.20 |
100.00 |
0.6000 |
-0.2344 |
298.20 |
100.00 |
0.6505 |
-0.2193 |
298.20 |
10000.00 |
0.2001 |
-0.1911 |
298.20 |
10000.00 |
0.2503 |
-0.2139 |
298.20 |
10000.00 |
0.3004 |
-0.2312 |
298.20 |
10000.00 |
0.3502 |
-0.2434 |
298.20 |
10000.00 |
0.3995 |
-0.2517 |
298.20 |
10000.00 |
0.4504 |
-0.2547 |
298.20 |
10000.00 |
0.5007 |
-0.2530 |
298.20 |
10000.00 |
0.5504 |
-0.2454 |
298.20 |
10000.00 |
0.5994 |
-0.2344 |
298.20 |
10000.00 |
0.6497 |
-0.2205 |
313.20 |
100.00 |
0.2984 |
-0.2512 |
313.20 |
100.00 |
0.3505 |
-0.2669 |
313.20 |
100.00 |
0.4012 |
-0.2762 |
313.20 |
100.00 |
0.4501 |
-0.2794 |
313.20 |
100.00 |
0.5004 |
-0.2771 |
313.20 |
100.00 |
0.5488 |
-0.2686 |
313.20 |
100.00 |
0.5985 |
-0.2565 |
313.20 |
100.00 |
0.6497 |
-0.2389 |
313.20 |
100.00 |
0.6986 |
-0.2167 |
313.20 |
100.00 |
0.7488 |
-0.1904 |
313.20 |
100.00 |
0.8005 |
-0.1578 |
313.20 |
100.00 |
0.8495 |
-0.1244 |
313.20 |
10000.00 |
0.2492 |
-0.2313 |
313.20 |
10000.00 |
0.2998 |
-0.2555 |
313.20 |
10000.00 |
0.3489 |
-0.2701 |
313.20 |
10000.00 |
0.3995 |
-0.2792 |
313.20 |
10000.00 |
0.4484 |
-0.2820 |
313.20 |
10000.00 |
0.4986 |
-0.2802 |
313.20 |
10000.00 |
0.5504 |
-0.2718 |
313.20 |
10000.00 |
0.6001 |
-0.2584 |
313.20 |
10000.00 |
0.6512 |
-0.2396 |
313.20 |
10000.00 |
0.7000 |
-0.2166 |
313.20 |
10000.00 |
0.7501 |
-0.1894 |
313.20 |
10000.00 |
0.8015 |
-0.1567 |
313.20 |
10000.00 |
0.8503 |
-0.1228 |
328.20 |
100.00 |
0.2007 |
-0.2644 |
328.20 |
100.00 |
0.2509 |
-0.2912 |
328.20 |
100.00 |
0.3008 |
-0.3129 |
328.20 |
100.00 |
0.3505 |
-0.3269 |
328.20 |
100.00 |
0.3999 |
-0.3330 |
328.20 |
100.00 |
0.4507 |
-0.3333 |
328.20 |
100.00 |
0.4990 |
-0.3269 |
328.20 |
100.00 |
0.5509 |
-0.3133 |
328.20 |
100.00 |
0.6000 |
-0.2957 |
328.20 |
100.00 |
0.6505 |
-0.2721 |
328.20 |
100.00 |
0.7001 |
-0.2448 |
328.20 |
10000.00 |
0.2001 |
-0.2636 |
328.20 |
10000.00 |
0.2503 |
-0.2932 |
328.20 |
10000.00 |
0.3004 |
-0.3167 |
328.20 |
10000.00 |
0.3502 |
-0.3306 |
328.20 |
10000.00 |
0.3995 |
-0.3382 |
328.20 |
10000.00 |
0.4504 |
-0.3393 |
328.20 |
10000.00 |
0.5007 |
-0.3318 |
328.20 |
10000.00 |
0.5504 |
-0.3195 |
328.20 |
10000.00 |
0.5994 |
-0.3022 |
328.20 |
10000.00 |
0.6497 |
-0.2792 |
Sources