Operational conditions:
Fixed | Measured | |
---|---|---|
Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (2) - Liquid | Mole fraction of Benzene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.2500 | 0.0994 | 0.2464 |
0.2500 | 0.2000 | 0.4840 |
0.2500 | 0.2994 | 0.6972 |
0.2500 | 0.3995 | 0.8800 |
0.2500 | 0.5002 | 1.0196 |
0.2500 | 0.6012 | 1.101 |
0.2500 | 0.7004 | 1.1078 |
0.2500 | 0.7994 | 1.023 |
0.2500 | 0.9000 | 0.7690 |
0.6667 | 0.0993 | 0.1985 |
0.6667 | 0.2007 | 0.3916 |
0.6667 | 0.3010 | 0.5641 |
0.6667 | 0.4001 | 0.7095 |
0.6667 | 0.4995 | 0.8252 |
0.6667 | 0.6008 | 0.8980 |
0.6667 | 0.6994 | 0.9130 |
0.6667 | 0.8002 | 0.8433 |
0.6667 | 0.9006 | 0.6230 |
1.4997 | 0.0990 | 0.1556 |
1.4997 | 0.1993 | 0.3057 |
1.4997 | 0.2999 | 0.4444 |
1.4997 | 0.3999 | 0.5619 |
1.4997 | 0.5005 | 0.6559 |
1.4997 | 0.6009 | 0.7144 |
1.4997 | 0.6999 | 0.7250 |
1.4997 | 0.7999 | 0.6631 |
1.4997 | 0.8995 | 0.4745 |
4.0022 | 0.0995 | 0.1181 |
4.0022 | 0.1998 | 0.2302 |
4.0022 | 0.2995 | 0.3328 |
4.0022 | 0.4000 | 0.4196 |
4.0022 | 0.4998 | 0.4845 |
4.0022 | 0.5997 | 0.5224 |
4.0022 | 0.6998 | 0.5198 |
4.0022 | 0.8000 | 0.4587 |
4.0022 | 0.8995 | 0.3060 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (2) - Liquid | Mole fraction of Benzene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.2500 | 0.1006 | 0.2045 |
0.2500 | 0.2000 | 0.3997 |
0.2500 | 0.3004 | 0.5810 |
0.2500 | 0.4004 | 0.7364 |
0.2500 | 0.5000 | 0.8581 |
0.2500 | 0.6000 | 0.9316 |
0.2500 | 0.7001 | 0.9427 |
0.2500 | 0.8002 | 0.8741 |
0.2500 | 0.9000 | 0.6730 |
0.6667 | 0.1006 | 0.1720 |
0.6667 | 0.2007 | 0.3355 |
0.6667 | 0.2999 | 0.4838 |
0.6667 | 0.4001 | 0.6112 |
0.6667 | 0.5005 | 0.7134 |
0.6667 | 0.5998 | 0.7781 |
0.6667 | 0.7003 | 0.7935 |
0.6667 | 0.8002 | 0.7399 |
0.6667 | 0.8999 | 0.5651 |
1.4998 | 0.1005 | 0.1428 |
1.4998 | 0.2007 | 0.2770 |
1.4998 | 0.2999 | 0.3986 |
1.4998 | 0.3998 | 0.5043 |
1.4998 | 0.5005 | 0.5885 |
1.4998 | 0.5999 | 0.6426 |
1.4998 | 0.6998 | 0.6558 |
1.4998 | 0.7999 | 0.6070 |
1.4998 | 0.9002 | 0.4492 |
3.9975 | 0.0996 | 0.1128 |
3.9975 | 0.1998 | 0.2210 |
3.9975 | 0.3007 | 0.3193 |
3.9975 | 0.3999 | 0.4012 |
3.9975 | 0.4997 | 0.4648 |
3.9975 | 0.5996 | 0.5030 |
3.9975 | 0.6997 | 0.5050 |
3.9975 | 0.7999 | 0.4527 |
3.9975 | 0.9002 | 0.3104 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (2) - Liquid | Mole fraction of Benzene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.2500 | 0.0994 | 0.2464 |
0.2500 | 0.2000 | 0.4840 |
0.2500 | 0.2994 | 0.6972 |
0.2500 | 0.3995 | 0.8800 |
0.2500 | 0.5002 | 1.0196 |
0.2500 | 0.6012 | 1.101 |
0.2500 | 0.7004 | 1.1078 |
0.2500 | 0.7994 | 1.023 |
0.2500 | 0.9000 | 0.7690 |
0.6667 | 0.0993 | 0.1985 |
0.6667 | 0.2007 | 0.3916 |
0.6667 | 0.3010 | 0.5641 |
0.6667 | 0.4001 | 0.7095 |
0.6667 | 0.4995 | 0.8252 |
0.6667 | 0.6008 | 0.8980 |
0.6667 | 0.6994 | 0.9130 |
0.6667 | 0.8002 | 0.8433 |
0.6667 | 0.9006 | 0.6230 |
1.4997 | 0.0990 | 0.1556 |
1.4997 | 0.1993 | 0.3057 |
1.4997 | 0.2999 | 0.4444 |
1.4997 | 0.3999 | 0.5619 |
1.4997 | 0.5005 | 0.6559 |
1.4997 | 0.6009 | 0.7144 |
1.4997 | 0.6999 | 0.7250 |
1.4997 | 0.7999 | 0.6631 |
1.4997 | 0.8995 | 0.4745 |
4.0022 | 0.0995 | 0.1181 |
4.0022 | 0.1998 | 0.2302 |
4.0022 | 0.2995 | 0.3328 |
4.0022 | 0.4000 | 0.4196 |
4.0022 | 0.4998 | 0.4845 |
4.0022 | 0.5997 | 0.5224 |
4.0022 | 0.6998 | 0.5198 |
4.0022 | 0.8000 | 0.4587 |
4.0022 | 0.8995 | 0.3060 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (2) - Liquid | Mole fraction of Benzene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.2500 | 0.1006 | 0.2045 |
0.2500 | 0.2000 | 0.3997 |
0.2500 | 0.3004 | 0.5810 |
0.2500 | 0.4004 | 0.7364 |
0.2500 | 0.5000 | 0.8581 |
0.2500 | 0.6000 | 0.9316 |
0.2500 | 0.7001 | 0.9427 |
0.2500 | 0.8002 | 0.8741 |
0.2500 | 0.9000 | 0.6730 |
0.6667 | 0.1006 | 0.1720 |
0.6667 | 0.2007 | 0.3355 |
0.6667 | 0.2999 | 0.4838 |
0.6667 | 0.4001 | 0.6112 |
0.6667 | 0.5005 | 0.7134 |
0.6667 | 0.5998 | 0.7781 |
0.6667 | 0.7003 | 0.7935 |
0.6667 | 0.8002 | 0.7399 |
0.6667 | 0.8999 | 0.5651 |
1.4998 | 0.1005 | 0.1428 |
1.4998 | 0.2007 | 0.2770 |
1.4998 | 0.2999 | 0.3986 |
1.4998 | 0.3998 | 0.5043 |
1.4998 | 0.5005 | 0.5885 |
1.4998 | 0.5999 | 0.6426 |
1.4998 | 0.6998 | 0.6558 |
1.4998 | 0.7999 | 0.6070 |
1.4998 | 0.9002 | 0.4492 |
3.9975 | 0.0996 | 0.1128 |
3.9975 | 0.1998 | 0.2210 |
3.9975 | 0.3007 | 0.3193 |
3.9975 | 0.3999 | 0.4012 |
3.9975 | 0.4997 | 0.4648 |
3.9975 | 0.5996 | 0.5030 |
3.9975 | 0.6997 | 0.5050 |
3.9975 | 0.7999 | 0.4527 |
3.9975 | 0.9002 | 0.3104 |