Mixture of Isopropyl Alcohol + 1,2-Propanediamine

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

1,2-Propanediamine

Name
1,2-Propanediamine
InChI
InChI=1S/C3H10N2/c1-3(5)2-4/h3H,2,4-5H2,1H3
InChI Key
AOHJOMMDDJHIJH-UHFFFAOYSA-N
Formula
C3H10N2
SMILES
CC(N)CN
Mol. Weight (g/mol)
74.12
CAS
78-90-0
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Isopropyl Alcohol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0095 -0.0559
0.0169 -0.1105
0.0243 -0.1634
0.0315 -0.2156
0.0386 -0.2659
0.0456 -0.3152
0.0526 -0.3634
0.0594 -0.4119
0.0661 -0.4592
0.0727 -0.5054
0.0793 -0.5504
0.0857 -0.5950
0.0921 -0.6386
0.0983 -0.6811
0.1045 -0.7233
0.1106 -0.7643
0.1166 -0.8049
0.1225 -0.8451
0.1284 -0.8840
0.1342 -0.9217
0.1413 -0.9633
0.1469 -0.9987
0.1524 -1.0372
0.1579 -1.0732
0.1633 -1.1054
0.1686 -1.1394
0.1738 -1.1764
0.1790 -1.205
0.1842 -1.2375
0.1892 -1.2692
0.1942 -1.3004
0.1992 -1.3306
0.2040 -1.3601
0.2088 -1.3896
0.2136 -1.4178
0.2183 -1.4458
0.2230 -1.4731
0.2276 -1.5003
0.2321 -1.5266
0.2366 -1.5518
0.2421 -1.5742
0.2465 -1.5995
0.2508 -1.6235
0.2551 -1.6475
0.2593 -1.6702
0.2635 -1.6931
0.2676 -1.7155
0.2717 -1.7377
0.2757 -1.7595
0.2797 -1.7789
0.2837 -1.8002
0.2876 -1.8131
0.2914 -1.8339
0.2952 -1.8541
0.3028 -1.8888
0.3065 -1.9052
0.3131 -1.9359
0.3192 -1.9632
0.3253 -1.9906
0.3312 -2.0138
0.3371 -2.0402
0.3428 -2.0609
0.3485 -2.0807
0.3540 -2.1004
0.3595 -2.1191
0.3648 -2.1373
0.3701 -2.1547
0.3753 -2.1712
0.3804 -2.1893
0.3854 -2.2079
0.3903 -2.2237
0.3952 -2.2426
0.4000 -2.2564
0.4047 -2.2699
0.4093 -2.2832
0.4139 -2.2961
0.4228 -2.3212
0.4315 -2.3446
0.4398 -2.3659
0.4480 -2.3857
0.4559 -2.3984
0.4636 -2.4188
0.4711 -2.4294
0.4784 -2.4454
0.4854 -2.4564
0.4923 -2.4651
0.4990 -2.4757
0.5055 -2.4849
0.5104 -2.4935
0.5119 -2.4932
0.5181 -2.5006
0.5242 -2.5073
0.5280 -2.5109
0.5300 -2.5132
0.5358 -2.5181
0.5414 -2.5226
0.5445 -2.5244
0.5469 -2.5264
0.5522 -2.5292
0.5575 -2.5314
0.5598 -2.5293
0.5626 -2.5331
0.5675 -2.5301
0.5742 -2.5294
0.5876 -2.5271
0.6002 -2.5211
0.6121 -2.5118
0.6233 -2.4992
0.6338 -2.4841
0.6438 -2.468
0.6533 -2.4501
0.6622 -2.4359
0.6707 -2.4157
0.6788 -2.3993
0.6865 -2.3769
0.6939 -2.3542
0.7009 -2.3312
0.7076 -2.3079
0.7140 -2.2893
0.7201 -2.2706
0.7260 -2.2467
0.7316 -2.2228
0.7422 -2.1852
0.7678 -2.0694
0.7854 -1.9794
0.8005 -1.9023
0.8135 -1.8285
0.8250 -1.7593
0.8352 -1.6931
0.8442 -1.6304
0.8523 -1.5707
0.8596 -1.5144
0.8778 -1.3785
0.8815 -1.3471
0.8852 -1.3168
0.8890 -1.2852
0.8928 -1.2506
0.9005 -1.1785
0.9045 -1.1443
0.9084 -1.1027
0.9125 -1.0656
0.9164 -1.0222
0.9204 -0.9778
0.9245 -0.9373
0.9287 -0.8894
0.9287 -0.8894
0.9328 -0.8488
0.9328 -0.8488
0.9370 -0.7999
0.9412 -0.7566
0.9455 -0.7086
0.9498 -0.6584
0.9542 -0.6069
0.9586 -0.5544
0.9630 -0.4991
0.9675 -0.4435
0.9720 -0.3855
0.9766 -0.3268
0.9812 -0.2614
0.9858 -0.1948
0.9905 -0.1315
0.9952 -0.0667

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Isopropyl Alcohol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0095 -0.0559
0.0169 -0.1105
0.0243 -0.1634
0.0315 -0.2156
0.0386 -0.2659
0.0456 -0.3152
0.0526 -0.3634
0.0594 -0.4119
0.0661 -0.4592
0.0727 -0.5054
0.0793 -0.5504
0.0857 -0.5950
0.0921 -0.6386
0.0983 -0.6811
0.1045 -0.7233
0.1106 -0.7643
0.1166 -0.8049
0.1225 -0.8451
0.1284 -0.8840
0.1342 -0.9217
0.1413 -0.9633
0.1469 -0.9987
0.1524 -1.0372
0.1579 -1.0732
0.1633 -1.1054
0.1686 -1.1394
0.1738 -1.1764
0.1790 -1.205
0.1842 -1.2375
0.1892 -1.2692
0.1942 -1.3004
0.1992 -1.3306
0.2040 -1.3601
0.2088 -1.3896
0.2136 -1.4178
0.2183 -1.4458
0.2230 -1.4731
0.2276 -1.5003
0.2321 -1.5266
0.2366 -1.5518
0.2421 -1.5742
0.2465 -1.5995
0.2508 -1.6235
0.2551 -1.6475
0.2593 -1.6702
0.2635 -1.6931
0.2676 -1.7155
0.2717 -1.7377
0.2757 -1.7595
0.2797 -1.7789
0.2837 -1.8002
0.2876 -1.8131
0.2914 -1.8339
0.2952 -1.8541
0.3028 -1.8888
0.3065 -1.9052
0.3131 -1.9359
0.3192 -1.9632
0.3253 -1.9906
0.3312 -2.0138
0.3371 -2.0402
0.3428 -2.0609
0.3485 -2.0807
0.3540 -2.1004
0.3595 -2.1191
0.3648 -2.1373
0.3701 -2.1547
0.3753 -2.1712
0.3804 -2.1893
0.3854 -2.2079
0.3903 -2.2237
0.3952 -2.2426
0.4000 -2.2564
0.4047 -2.2699
0.4093 -2.2832
0.4139 -2.2961
0.4228 -2.3212
0.4315 -2.3446
0.4398 -2.3659
0.4480 -2.3857
0.4559 -2.3984
0.4636 -2.4188
0.4711 -2.4294
0.4784 -2.4454
0.4854 -2.4564
0.4923 -2.4651
0.4990 -2.4757
0.5055 -2.4849
0.5104 -2.4935
0.5119 -2.4932
0.5181 -2.5006
0.5242 -2.5073
0.5280 -2.5109
0.5300 -2.5132
0.5358 -2.5181
0.5414 -2.5226
0.5445 -2.5244
0.5469 -2.5264
0.5522 -2.5292
0.5575 -2.5314
0.5598 -2.5293
0.5626 -2.5331
0.5675 -2.5301
0.5742 -2.5294
0.5876 -2.5271
0.6002 -2.5211
0.6121 -2.5118
0.6233 -2.4992
0.6338 -2.4841
0.6438 -2.468
0.6533 -2.4501
0.6622 -2.4359
0.6707 -2.4157
0.6788 -2.3993
0.6865 -2.3769
0.6939 -2.3542
0.7009 -2.3312
0.7076 -2.3079
0.7140 -2.2893
0.7201 -2.2706
0.7260 -2.2467
0.7316 -2.2228
0.7422 -2.1852
0.7678 -2.0694
0.7854 -1.9794
0.8005 -1.9023
0.8135 -1.8285
0.8250 -1.7593
0.8352 -1.6931
0.8442 -1.6304
0.8523 -1.5707
0.8596 -1.5144
0.8778 -1.3785
0.8815 -1.3471
0.8852 -1.3168
0.8890 -1.2852
0.8928 -1.2506
0.9005 -1.1785
0.9045 -1.1443
0.9084 -1.1027
0.9125 -1.0656
0.9164 -1.0222
0.9204 -0.9778
0.9245 -0.9373
0.9287 -0.8894
0.9287 -0.8894
0.9328 -0.8488
0.9328 -0.8488
0.9370 -0.7999
0.9412 -0.7566
0.9455 -0.7086
0.9498 -0.6584
0.9542 -0.6069
0.9586 -0.5544
0.9630 -0.4991
0.9675 -0.4435
0.9720 -0.3855
0.9766 -0.3268
0.9812 -0.2614
0.9858 -0.1948
0.9905 -0.1315
0.9952 -0.0667

Sources