Mixture of n-Butyl ether + 1-Butanol + Heptane

Excel

n-Butyl ether

Name
n-Butyl ether
InChI
InChI=1S/C8H18O/c1-3-5-7-9-8-6-4-2/h3-8H2,1-2H3
InChI Key
DURPTKYDGMDSBL-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCOCCCC
Mol. Weight (g/mol)
130.23
CAS
142-96-1

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Excess molar enthalpy (molar enthalpy (2)

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

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Heptane (3) - Liquid Mole fraction of 1-Butanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0996 0.5403 0.8038
298.15 0.0998 0.5854 0.5385
298.15 0.1002 0.1799 0.7726
298.15 0.1014 0.3591 0.8945
298.15 0.1996 0.4803 0.8273
298.15 0.1996 0.5379 0.6144
298.15 0.2005 0.1598 0.7598
298.15 0.2021 0.3188 0.8866
298.15 0.2997 0.4202 0.8324
298.15 0.2997 0.4881 0.6711
298.15 0.2998 0.1400 0.7350
298.15 0.3030 0.2785 0.8623
298.15 0.3999 0.3601 0.8196
298.15 0.4002 0.1199 0.6977
298.15 0.4002 0.4348 0.7062
298.15 0.4033 0.2384 0.8202
298.15 0.4995 0.3794 0.7135
298.15 0.4997 0.1000 0.6481
298.15 0.4999 0.3001 0.7831
298.15 0.5037 0.1983 0.7652
298.15 0.5994 0.2404 0.7301
298.15 0.5999 0.3193 0.6982
298.15 0.6003 0.0799 0.5848
298.15 0.6035 0.1584 0.6958
298.15 0.6994 0.1804 0.6561
298.15 0.6999 0.0600 0.5059
298.15 0.7000 0.2532 0.6534
298.15 0.7034 0.1185 0.6100
298.15 0.7996 0.0401 0.4111
298.15 0.7996 0.1203 0.5560
298.15 0.8002 0.1850 0.5733
298.15 0.8025 0.0789 0.5046
298.15 0.8999 0.0601 0.4171
298.15 0.9000 0.0800 0.4451
298.15 0.9003 0.0199 0.2831
298.15 0.9018 0.0392 0.3660
313.15 0.0997 0.5402 0.9530
313.15 0.0999 0.7201 0.6574
313.15 0.1003 0.1798 0.8987
313.15 0.1005 0.3597 1.0539
313.15 0.1997 0.1599 0.8863
313.15 0.1997 0.4802 0.9937
313.15 0.1998 0.6402 0.7665
313.15 0.2003 0.3198 1.0526
313.15 0.2998 0.5602 0.8477
313.15 0.2999 0.4201 1.0114
313.15 0.3000 0.1399 0.8608
313.15 0.3004 0.2798 1.0341
313.15 0.4001 0.3599 1.0072
313.15 0.4003 0.4798 0.9017
313.15 0.4004 0.1198 0.8216
313.15 0.4005 0.2398 0.9984
313.15 0.4996 0.4004 0.9249
313.15 0.4999 0.0999 0.7698
313.15 0.5001 0.1999 0.9456
313.15 0.5001 0.2999 0.9806
313.15 0.5996 0.2402 0.9297
313.15 0.5997 0.1601 0.8750
313.15 0.6000 0.3200 0.9156
313.15 0.6005 0.0798 0.7013
313.15 0.6995 0.1202 0.7829
313.15 0.6995 0.1803 0.8519
313.15 0.7000 0.2400 0.8670
313.15 0.7001 0.0599 0.6164
313.15 0.7996 0.0801 0.6625
313.15 0.7996 0.1202 0.7391
313.15 0.7997 0.0400 0.5053
313.15 0.8002 0.1599 0.7753
313.15 0.8998 0.0401 0.4856
313.15 0.8999 0.0601 0.5652
313.15 0.8999 0.0801 0.6142
313.15 0.9004 0.0199 0.3406

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

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Heptane (3) - Liquid Mole fraction of 1-Butanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0996 0.5403 0.8038
298.15 0.0998 0.5854 0.5385
298.15 0.1002 0.1799 0.7726
298.15 0.1014 0.3591 0.8945
298.15 0.1996 0.4803 0.8273
298.15 0.1996 0.5379 0.6144
298.15 0.2005 0.1598 0.7598
298.15 0.2021 0.3188 0.8866
298.15 0.2997 0.4202 0.8324
298.15 0.2997 0.4881 0.6711
298.15 0.2998 0.1400 0.7350
298.15 0.3030 0.2785 0.8623
298.15 0.3999 0.3601 0.8196
298.15 0.4002 0.1199 0.6977
298.15 0.4002 0.4348 0.7062
298.15 0.4033 0.2384 0.8202
298.15 0.4995 0.3794 0.7135
298.15 0.4997 0.1000 0.6481
298.15 0.4999 0.3001 0.7831
298.15 0.5037 0.1983 0.7652
298.15 0.5994 0.2404 0.7301
298.15 0.5999 0.3193 0.6982
298.15 0.6003 0.0799 0.5848
298.15 0.6035 0.1584 0.6958
298.15 0.6994 0.1804 0.6561
298.15 0.6999 0.0600 0.5059
298.15 0.7000 0.2532 0.6534
298.15 0.7034 0.1185 0.6100
298.15 0.7996 0.0401 0.4111
298.15 0.7996 0.1203 0.5560
298.15 0.8002 0.1850 0.5733
298.15 0.8025 0.0789 0.5046
298.15 0.8999 0.0601 0.4171
298.15 0.9000 0.0800 0.4451
298.15 0.9003 0.0199 0.2831
298.15 0.9018 0.0392 0.3660
313.15 0.0997 0.5402 0.9530
313.15 0.0999 0.7201 0.6574
313.15 0.1003 0.1798 0.8987
313.15 0.1005 0.3597 1.0539
313.15 0.1997 0.1599 0.8863
313.15 0.1997 0.4802 0.9937
313.15 0.1998 0.6402 0.7665
313.15 0.2003 0.3198 1.0526
313.15 0.2998 0.5602 0.8477
313.15 0.2999 0.4201 1.0114
313.15 0.3000 0.1399 0.8608
313.15 0.3004 0.2798 1.0341
313.15 0.4001 0.3599 1.0072
313.15 0.4003 0.4798 0.9017
313.15 0.4004 0.1198 0.8216
313.15 0.4005 0.2398 0.9984
313.15 0.4996 0.4004 0.9249
313.15 0.4999 0.0999 0.7698
313.15 0.5001 0.1999 0.9456
313.15 0.5001 0.2999 0.9806
313.15 0.5996 0.2402 0.9297
313.15 0.5997 0.1601 0.8750
313.15 0.6000 0.3200 0.9156
313.15 0.6005 0.0798 0.7013
313.15 0.6995 0.1202 0.7829
313.15 0.6995 0.1803 0.8519
313.15 0.7000 0.2400 0.8670
313.15 0.7001 0.0599 0.6164
313.15 0.7996 0.0801 0.6625
313.15 0.7996 0.1202 0.7391
313.15 0.7997 0.0400 0.5053
313.15 0.8002 0.1599 0.7753
313.15 0.8998 0.0401 0.4856
313.15 0.8999 0.0601 0.5652
313.15 0.8999 0.0801 0.6142
313.15 0.9004 0.0199 0.3406

Sources