Mixture of Butanamide + Water

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Butanamide

Name
Butanamide
InChI
InChI=1S/C4H9NO/c1-2-3-4(5)6/h2-3H2,1H3,(H2,5,6)
InChI Key
DNSISZSEWVHGLH-UHFFFAOYSA-N
Formula
C4H9NO
SMILES
CCCC(N)=O
Mol. Weight (g/mol)
87.12
CAS
541-35-5

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Mole fraction (2)
  2. Molar enthalpy (2)
  3. ρl - Mass density, kg/m3 (2)

Mole fraction of Butanamide (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Temperature, K - Liquid Mole fraction of Butanamide (1) - Liquid
278.15 0.0163
283.15 0.0210
288.15 0.0260
293.15 0.0331
298.15 0.0442
303.15 0.0575
308.15 0.0724
313.15 0.0895
318.15 0.1089
323.15 0.1305
328.15 0.1524
333.15 0.1748

Mole fraction of Butanamide (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Temperature, K - Liquid Mole fraction of Butanamide (1) - Liquid
278.15 0.0163
283.15 0.0210
288.15 0.0260
293.15 0.0331
298.15 0.0442
303.15 0.0575
308.15 0.0724
313.15 0.0895
318.15 0.1089
323.15 0.1305
328.15 0.1524
333.15 0.1748

Molar enthalpy of dilution, kJ/mol [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Initial molality of solute, mol/kg - Liquid Final molality of solute, mol/kg - Liquid Molar enthalpy of dilution, kJ/mol - Liquid
293.15 0.1997 0.0919 0.0637
293.15 0.4022 0.1835 0.1021
293.15 0.6000 0.2712 0.1842
293.15 0.8001 0.3584 0.2759
293.15 1.0021 0.4448 0.3492
293.15 1.1997 0.5279 0.4116
293.15 1.3988 0.6101 0.5178
293.15 1.5999 0.6918 0.5974
293.15 1.7943 0.7693 0.6498
293.15 1.9951 0.8481 0.7265
293.15 2.5007 1.0406 0.9436
293.15 2.9995 1.2227 1.1572
298.15 0.2000 0.0921 0.0390
298.15 0.4031 0.1838 0.1155
298.15 0.6004 0.2714 0.1878
298.15 0.8002 0.3584 0.2723
298.15 0.9993 0.4436 0.3423
298.15 1.1946 0.5718 0.3968
298.15 1.398 0.6098 0.5014
298.15 1.5998 0.6917 0.5831
298.15 1.8001 0.8407 0.6250
298.15 1.9992 0.8497 0.7315
298.15 2.496 1.0388 0.9458
298.15 2.9987 1.2224 1.1417
303.15 0.2002 0.1004 0.0457
303.15 0.3948 0.1964 0.1026
303.15 0.5996 0.2957 0.1660
303.15 0.8036 0.3930 0.2332
303.15 0.9973 0.4838 0.2984
303.15 1.2032 0.5788 0.3730
303.15 1.4028 0.6693 0.4458
303.15 1.6004 0.7575 0.5161
303.15 1.8011 0.8457 0.5887
303.15 1.9993 0.9313 0.6602
303.15 2.4385 1.1165 0.8052
303.15 2.9987 1.3436 0.9905
308.15 0.1996 0.0919 0.0442
308.15 0.4008 0.1828 0.1001
308.15 0.6013 0.2718 0.1737
308.15 0.8010 0.3588 0.2487
308.15 0.9991 0.4435 0.3119
308.15 1.1973 0.5269 0.3856
308.15 1.4001 0.6107 0.4600
308.15 1.6003 0.6919 0.5323
308.15 1.7993 0.7713 0.6038
308.15 1.9975 0.8490 0.6679
308.15 2.4989 1.0399 0.8485
308.15 2.9906 1.2195 0.9964

Molar enthalpy of dilution, kJ/mol [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Initial molality of solute, mol/kg - Liquid Final molality of solute, mol/kg - Liquid Molar enthalpy of dilution, kJ/mol - Liquid
293.15 0.1997 0.0919 0.0637
293.15 0.4022 0.1835 0.1021
293.15 0.6000 0.2712 0.1842
293.15 0.8001 0.3584 0.2759
293.15 1.0021 0.4448 0.3492
293.15 1.1997 0.5279 0.4116
293.15 1.3988 0.6101 0.5178
293.15 1.5999 0.6918 0.5974
293.15 1.7943 0.7693 0.6498
293.15 1.9951 0.8481 0.7265
293.15 2.5007 1.0406 0.9436
293.15 2.9995 1.2227 1.1572
298.15 0.2000 0.0921 0.0390
298.15 0.4031 0.1838 0.1155
298.15 0.6004 0.2714 0.1878
298.15 0.8002 0.3584 0.2723
298.15 0.9993 0.4436 0.3423
298.15 1.1946 0.5718 0.3968
298.15 1.398 0.6098 0.5014
298.15 1.5998 0.6917 0.5831
298.15 1.8001 0.8407 0.6250
298.15 1.9992 0.8497 0.7315
298.15 2.496 1.0388 0.9458
298.15 2.9987 1.2224 1.1417
303.15 0.2002 0.1004 0.0457
303.15 0.3948 0.1964 0.1026
303.15 0.5996 0.2957 0.1660
303.15 0.8036 0.3930 0.2332
303.15 0.9973 0.4838 0.2984
303.15 1.2032 0.5788 0.3730
303.15 1.4028 0.6693 0.4458
303.15 1.6004 0.7575 0.5161
303.15 1.8011 0.8457 0.5887
303.15 1.9993 0.9313 0.6602
303.15 2.4385 1.1165 0.8052
303.15 2.9987 1.3436 0.9905
308.15 0.1996 0.0919 0.0442
308.15 0.4008 0.1828 0.1001
308.15 0.6013 0.2718 0.1737
308.15 0.8010 0.3588 0.2487
308.15 0.9991 0.4435 0.3119
308.15 1.1973 0.5269 0.3856
308.15 1.4001 0.6107 0.4600
308.15 1.6003 0.6919 0.5323
308.15 1.7993 0.7713 0.6038
308.15 1.9975 0.8490 0.6679
308.15 2.4989 1.0399 0.8485
308.15 2.9906 1.2195 0.9964

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 75 (Liquid)

Fixed Measured
Temperature, K - Liquid Molality, mol/kg of Butanamide (1) - Liquid Mass density, kg/m3 - Liquid
275.66 0.1003 1000.061
275.66 0.1971 1000.2
275.66 0.3010 1000.371
275.66 0.4013 1000.561
275.66 0.4955 1000.746
275.66 0.6013 1000.974
275.66 0.6950 1001.198
275.66 0.8012 1001.461
276.14 0.1021 1000.06
276.14 0.1961 1000.202
276.14 0.2967 1000.37
276.14 0.4955 1000.747
276.14 0.6013 1000.964
276.14 0.6982 1001.181
276.14 0.8012 1001.421
276.14 0.9855 1001.868
276.61 0.1009 1000.048
276.61 0.1973 1000.178
276.61 0.2967 1000.332
276.61 0.4013 1000.51
276.61 0.5977 1000.895
276.61 0.7003 1001.11
276.61 0.8012 1001.345
276.61 0.9976 1001.83
277.15 0.1021 1000.092
277.15 0.1961 1000.207
277.15 0.2967 1000.345
277.15 0.4955 1000.691
277.15 0.6013 1000.903
277.15 0.6982 1001.132
277.15 0.8012 1001.397
277.15 0.9855 1001.938
277.61 0.1009 1000.084
277.61 0.1973 1000.211
277.61 0.2967 1000.361
277.61 0.4013 1000.529
277.61 0.5977 1000.891
277.61 0.7003 1001.104
277.61 0.8024 1001.323
277.61 0.9976 1001.768
278.12 0.1076 1000.073
278.12 0.1971 1000.191
278.12 0.3283 1000.378
278.12 0.4191 1000.51
278.12 0.5074 1000.654
278.12 0.6233 1000.845
278.12 0.7379 1001.039
278.12 0.8761 1001.282
278.68 0.1003 1000.049
278.68 0.1971 1000.168
278.68 0.3010 1000.312
278.68 0.4013 1000.462
278.68 0.4955 1000.619
278.68 0.6013 1000.813
278.68 0.6950 1001.003
278.68 0.8012 1001.228

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 75 (Liquid)

Fixed Measured
Temperature, K - Liquid Molality, mol/kg of Butanamide (1) - Liquid Mass density, kg/m3 - Liquid
275.66 0.1003 1000.061
275.66 0.1971 1000.2
275.66 0.3010 1000.371
275.66 0.4013 1000.561
275.66 0.4955 1000.746
275.66 0.6013 1000.974
275.66 0.6950 1001.198
275.66 0.8012 1001.461
276.14 0.1021 1000.06
276.14 0.1961 1000.202
276.14 0.2967 1000.37
276.14 0.4955 1000.747
276.14 0.6013 1000.964
276.14 0.6982 1001.181
276.14 0.8012 1001.421
276.14 0.9855 1001.868
276.61 0.1009 1000.048
276.61 0.1973 1000.178
276.61 0.2967 1000.332
276.61 0.4013 1000.51
276.61 0.5977 1000.895
276.61 0.7003 1001.11
276.61 0.8012 1001.345
276.61 0.9976 1001.83
277.15 0.1021 1000.092
277.15 0.1961 1000.207
277.15 0.2967 1000.345
277.15 0.4955 1000.691
277.15 0.6013 1000.903
277.15 0.6982 1001.132
277.15 0.8012 1001.397
277.15 0.9855 1001.938
277.61 0.1009 1000.084
277.61 0.1973 1000.211
277.61 0.2967 1000.361
277.61 0.4013 1000.529
277.61 0.5977 1000.891
277.61 0.7003 1001.104
277.61 0.8024 1001.323
277.61 0.9976 1001.768
278.12 0.1076 1000.073
278.12 0.1971 1000.191
278.12 0.3283 1000.378
278.12 0.4191 1000.51
278.12 0.5074 1000.654
278.12 0.6233 1000.845
278.12 0.7379 1001.039
278.12 0.8761 1001.282
278.68 0.1003 1000.049
278.68 0.1971 1000.168
278.68 0.3010 1000.312
278.68 0.4013 1000.462
278.68 0.4955 1000.619
278.68 0.6013 1000.813
278.68 0.6950 1001.003
278.68 0.8012 1001.228

Sources