Mixture of Diisopropyl ether + Carbon dioxide

Datasets

1. Mole fraction (4)
2. Excess molar enthalpy (molar enthalpy (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Gas
0.1127	293.15	0.9653
0.1154	333.15	0.9269
0.1235	313.15	0.9419
0.1728	333.15	0.9456
0.1831	273.15	0.9805
0.1946	313.15	0.9572
0.2281	293.15	0.9771
0.2668	333.15	0.9562
0.2728	313.15	0.9649
0.2795	265.15	0.9968
0.2961	293.15	0.9811
0.3091	273.15	0.9876
0.3447	333.15	0.9631
0.3666	313.15	0.9705
0.3754	265.15	0.9976
0.3828	333.15	0.9683
0.4015	293.15	0.9833
0.4024	313.15	0.9729
0.4361	273.15	0.9903
0.4907	293.15	0.9845
0.5112	265.15	0.9986
0.5756	273.15	0.9918
0.6450	273.15	0.9927
0.6565	265.15	0.9995
0.7589	265.15	0.9998

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
298.15	5000.00	0.8458
298.15	5500.00	0.9142
303.15	5000.00	0.7686
303.15	5500.00	0.8370
303.15	6000.00	0.8905
308.15	5000.00	0.7055
308.15	5500.00	0.7677
308.15	6000.00	0.8295
308.15	6500.00	0.8878
308.15	7000.00	0.9390
308.15	7500.00	0.9567

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Gas
0.1127	293.15	0.9653
0.1154	333.15	0.9269
0.1235	313.15	0.9419
0.1728	333.15	0.9456
0.1831	273.15	0.9805
0.1946	313.15	0.9572
0.2281	293.15	0.9771
0.2668	333.15	0.9562
0.2728	313.15	0.9649
0.2795	265.15	0.9968
0.2961	293.15	0.9811
0.3091	273.15	0.9876
0.3447	333.15	0.9631
0.3666	313.15	0.9705
0.3754	265.15	0.9976
0.3828	333.15	0.9683
0.4015	293.15	0.9833
0.4024	313.15	0.9729
0.4361	273.15	0.9903
0.4907	293.15	0.9845
0.5112	265.15	0.9986
0.5756	273.15	0.9918
0.6450	273.15	0.9927
0.6565	265.15	0.9995
0.7589	265.15	0.9998

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
298.15	5000.00	0.8458
298.15	5500.00	0.9142
303.15	5000.00	0.7686
303.15	5500.00	0.8370
303.15	6000.00	0.8905
308.15	5000.00	0.7055
308.15	5500.00	0.7677
308.15	6000.00	0.8295
308.15	6500.00	0.8878
308.15	7000.00	0.9390
308.15	7500.00	0.9567

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

Fixed			Measured
Mole fraction of Carbon dioxide (2) - Fluid (supercritical or subcritical phases)	Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Fluid (supercritical or subcritical phases)
0.1255	298.15	5000.00	-1.169
0.1255	303.15	5000.00	-1.05
0.1255	308.15	5000.00	-1.226
0.1263	298.15	5500.00	-1.158
0.1263	303.15	5500.00	-1.163
0.1263	308.15	5500.00	-1.15
0.1270	298.15	6000.00	-0.9720
0.1270	303.15	6000.00	-1.065
0.1270	308.15	6000.00	-1.158
0.1277	308.15	6500.00	-1.062
0.1283	308.15	7000.00	-0.9700
0.1289	308.15	7500.00	-0.8360
0.2326	298.15	5000.00	-2.203
0.2326	303.15	5000.00	-2.199
0.2326	308.15	5000.00	-2.218
0.2338	298.15	5500.00	-2.075
0.2338	303.15	5500.00	-2.114
0.2338	308.15	5500.00	-2.195
0.2350	298.15	6000.00	-1.848
0.2350	303.15	6000.00	-2.006
0.2350	308.15	6000.00	-2.065
0.2361	308.15	6500.00	-1.94
0.2370	308.15	7000.00	-1.761
0.2380	308.15	7500.00	-1.488
0.3249	298.15	5000.00	-3.069
0.3249	303.15	5000.00	-3.1
0.3249	308.15	5000.00	-3.118
0.3265	298.15	5500.00	-2.853
0.3265	303.15	5500.00	-2.991
0.3265	308.15	5500.00	-2.967
0.3279	298.15	6000.00	-2.597
0.3279	303.15	6000.00	-2.826
0.3279	308.15	6000.00	-2.899
0.3292	308.15	6500.00	-2.669
0.3304	308.15	7000.00	-2.458
0.3315	308.15	7500.00	-2.041
0.4054	298.15	5000.00	-3.822
0.4054	303.15	5000.00	-3.859
0.4054	308.15	5000.00	-3.865
0.4071	298.15	5500.00	-3.603
0.4071	303.15	5500.00	-3.685
0.4071	308.15	5500.00	-3.73
0.4087	298.15	6000.00	-3.184
0.4087	303.15	6000.00	-3.512
0.4087	308.15	6000.00	-3.571
0.4101	308.15	6500.00	-3.294
0.4114	308.15	7000.00	-3.046
0.4127	308.15	7500.00	-2.613
0.4762	298.15	5000.00	-4.493
0.4762	303.15	5000.00	-4.513
0.4762	308.15	5000.00	-4.562
0.4780	298.15	5500.00	-4.147
0.4780	303.15	5500.00	-4.301
0.4780	308.15	5500.00	-4.358
0.4796	298.15	6000.00	-3.723
0.4796	303.15	6000.00	-4.073
0.4796	308.15	6000.00	-4.276
0.4811	308.15	6500.00	-3.851
0.4824	308.15	7000.00	-3.587
0.4837	308.15	7500.00	-3.043
0.5389	298.15	5000.00	-5.026
0.5389	303.15	5000.00	-5.12
0.5389	308.15	5000.00	-5.118
0.5407	298.15	5500.00	-4.746
0.5407	303.15	5500.00	-4.861
0.5407	308.15	5500.00	-4.921
0.5423	298.15	6000.00	-4.218
0.5423	303.15	6000.00	-4.579
0.5423	308.15	6000.00	-4.695
0.5438	308.15	6500.00	-4.34
0.5451	308.15	7000.00	-3.976
0.5464	308.15	7500.00	-3.428
0.5949	298.15	5000.00	-5.585
0.5949	303.15	5000.00	-5.647
0.5949	308.15	5000.00	-5.619
0.5966	298.15	5500.00	-5.211
0.5966	303.15	5500.00	-5.353
0.5966	308.15	5500.00	-5.397
0.5982	298.15	6000.00	-4.575
0.5982	303.15	6000.00	-5.042
0.5982	308.15	6000.00	-5.115
0.5996	308.15	6500.00	-4.783
0.6009	308.15	7000.00	-4.399
0.6021	308.15	7500.00	-3.781
0.6452	298.15	5000.00	-6.05
0.6452	303.15	5000.00	-6.093
0.6452	308.15	5000.00	-6.072
0.6468	298.15	5500.00	-5.594
0.6468	303.15	5500.00	-5.773
0.6468	308.15	5500.00	-5.853
0.6483	298.15	6000.00	-4.959
0.6483	303.15	6000.00	-5.507
0.6483	308.15	6000.00	-5.611
0.6496	308.15	6500.00	-5.184
0.6509	308.15	7000.00	-4.748
0.6520	308.15	7500.00	-4.071
0.6906	298.15	5000.00	-6.479
0.6906	303.15	5000.00	-6.501
0.6906	308.15	5000.00	-6.474
0.6921	298.15	5500.00	-6.05
0.6921	303.15	5500.00	-6.177
0.6921	308.15	5500.00	-6.227
0.6934	298.15	6000.00	-5.311
0.6934	303.15	6000.00	-5.857
0.6934	308.15	6000.00	-5.941
0.6947	308.15	6500.00	-5.547
0.6958	308.15	7000.00	-5.077
0.6969	308.15	7500.00	-4.364
0.7317	298.15	5000.00	-6.796
0.7317	303.15	5000.00	-6.849
0.7331	298.15	5500.00	-6.375
0.7331	303.15	5500.00	-6.529
0.7331	308.15	5500.00	-6.576
0.7344	298.15	6000.00	-5.583
0.7344	303.15	6000.00	-6.174
0.7344	308.15	6000.00	-6.23
0.7355	308.15	6500.00	-5.804
0.7366	308.15	7000.00	-5.288
0.7376	308.15	7500.00	-4.613
0.7692	298.15	5000.00	-7.156
0.7705	298.15	5500.00	-6.747
0.7705	303.15	5500.00	-6.845
0.7716	298.15	6000.00	-5.843
0.7716	303.15	6000.00	-6.449
0.7716	308.15	6000.00	-6.528
0.7727	308.15	6500.00	-6.056
0.7736	308.15	7000.00	-5.562
0.7745	308.15	7500.00	-4.798
0.8036	298.15	5000.00	-7.495
0.8047	298.15	5500.00	-6.996
0.8047	303.15	5500.00	-7.083
0.8057	298.15	6000.00	-6.172
0.8057	303.15	6000.00	-6.703
0.8057	308.15	6000.00	-6.728
0.8066	308.15	6500.00	-6.267
0.8075	308.15	7000.00	-5.776
0.8083	308.15	7500.00	-4.971
0.8248	308.15	6000.00	-6.851
0.8351	298.15	5000.00	-7.726
0.8361	298.15	5500.00	-7.264
0.8370	298.15	6000.00	-6.37
0.8370	303.15	6000.00	-6.956
0.8378	308.15	6500.00	-6.522
0.8385	308.15	7000.00	-5.928
0.8392	308.15	7500.00	-5.178
0.8650	298.15	5500.00	-7.436
0.8658	298.15	6000.00	-6.637
0.8658	303.15	6000.00	-7.126
0.8665	308.15	6500.00	-6.705
0.8671	308.15	7000.00	-6.02
0.8677	308.15	7500.00	-5.25
0.8918	298.15	5500.00	-7.621
0.8924	298.15	6000.00	-6.806
0.8924	303.15	6000.00	-7.157
0.8935	308.15	7000.00	-6.098
0.8940	308.15	7500.00	-5.358
0.9019	298.15	5500.00	-7.673
0.9171	298.15	6000.00	-6.921
0.9179	308.15	7000.00	-6.144
0.9183	308.15	7500.00	-5.251
0.9310	298.15	6000.00	-6.837
0.9400	298.15	6000.00	-6.969
0.9409	308.15	7500.00	-5.174
0.9614	298.15	6000.00	-6.872
0.9620	308.15	7500.00	-4.909
0.9813	298.15	6000.00	-6.209

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

Fixed			Measured
Mole fraction of Carbon dioxide (2) - Fluid (supercritical or subcritical phases)	Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Fluid (supercritical or subcritical phases)
0.1255	298.15	5000.00	-1.169
0.1255	303.15	5000.00	-1.05
0.1255	308.15	5000.00	-1.226
0.1263	298.15	5500.00	-1.158
0.1263	303.15	5500.00	-1.163
0.1263	308.15	5500.00	-1.15
0.1270	298.15	6000.00	-0.9720
0.1270	303.15	6000.00	-1.065
0.1270	308.15	6000.00	-1.158
0.1277	308.15	6500.00	-1.062
0.1283	308.15	7000.00	-0.9700
0.1289	308.15	7500.00	-0.8360
0.2326	298.15	5000.00	-2.203
0.2326	303.15	5000.00	-2.199
0.2326	308.15	5000.00	-2.218
0.2338	298.15	5500.00	-2.075
0.2338	303.15	5500.00	-2.114
0.2338	308.15	5500.00	-2.195
0.2350	298.15	6000.00	-1.848
0.2350	303.15	6000.00	-2.006
0.2350	308.15	6000.00	-2.065
0.2361	308.15	6500.00	-1.94
0.2370	308.15	7000.00	-1.761
0.2380	308.15	7500.00	-1.488
0.3249	298.15	5000.00	-3.069
0.3249	303.15	5000.00	-3.1
0.3249	308.15	5000.00	-3.118
0.3265	298.15	5500.00	-2.853
0.3265	303.15	5500.00	-2.991
0.3265	308.15	5500.00	-2.967
0.3279	298.15	6000.00	-2.597
0.3279	303.15	6000.00	-2.826
0.3279	308.15	6000.00	-2.899
0.3292	308.15	6500.00	-2.669
0.3304	308.15	7000.00	-2.458
0.3315	308.15	7500.00	-2.041
0.4054	298.15	5000.00	-3.822
0.4054	303.15	5000.00	-3.859
0.4054	308.15	5000.00	-3.865
0.4071	298.15	5500.00	-3.603
0.4071	303.15	5500.00	-3.685
0.4071	308.15	5500.00	-3.73
0.4087	298.15	6000.00	-3.184
0.4087	303.15	6000.00	-3.512
0.4087	308.15	6000.00	-3.571
0.4101	308.15	6500.00	-3.294
0.4114	308.15	7000.00	-3.046
0.4127	308.15	7500.00	-2.613
0.4762	298.15	5000.00	-4.493
0.4762	303.15	5000.00	-4.513
0.4762	308.15	5000.00	-4.562
0.4780	298.15	5500.00	-4.147
0.4780	303.15	5500.00	-4.301
0.4780	308.15	5500.00	-4.358
0.4796	298.15	6000.00	-3.723
0.4796	303.15	6000.00	-4.073
0.4796	308.15	6000.00	-4.276
0.4811	308.15	6500.00	-3.851
0.4824	308.15	7000.00	-3.587
0.4837	308.15	7500.00	-3.043
0.5389	298.15	5000.00	-5.026
0.5389	303.15	5000.00	-5.12
0.5389	308.15	5000.00	-5.118
0.5407	298.15	5500.00	-4.746
0.5407	303.15	5500.00	-4.861
0.5407	308.15	5500.00	-4.921
0.5423	298.15	6000.00	-4.218
0.5423	303.15	6000.00	-4.579
0.5423	308.15	6000.00	-4.695
0.5438	308.15	6500.00	-4.34
0.5451	308.15	7000.00	-3.976
0.5464	308.15	7500.00	-3.428
0.5949	298.15	5000.00	-5.585
0.5949	303.15	5000.00	-5.647
0.5949	308.15	5000.00	-5.619
0.5966	298.15	5500.00	-5.211
0.5966	303.15	5500.00	-5.353
0.5966	308.15	5500.00	-5.397
0.5982	298.15	6000.00	-4.575
0.5982	303.15	6000.00	-5.042
0.5982	308.15	6000.00	-5.115
0.5996	308.15	6500.00	-4.783
0.6009	308.15	7000.00	-4.399
0.6021	308.15	7500.00	-3.781
0.6452	298.15	5000.00	-6.05
0.6452	303.15	5000.00	-6.093
0.6452	308.15	5000.00	-6.072
0.6468	298.15	5500.00	-5.594
0.6468	303.15	5500.00	-5.773
0.6468	308.15	5500.00	-5.853
0.6483	298.15	6000.00	-4.959
0.6483	303.15	6000.00	-5.507
0.6483	308.15	6000.00	-5.611
0.6496	308.15	6500.00	-5.184
0.6509	308.15	7000.00	-4.748
0.6520	308.15	7500.00	-4.071
0.6906	298.15	5000.00	-6.479
0.6906	303.15	5000.00	-6.501
0.6906	308.15	5000.00	-6.474
0.6921	298.15	5500.00	-6.05
0.6921	303.15	5500.00	-6.177
0.6921	308.15	5500.00	-6.227
0.6934	298.15	6000.00	-5.311
0.6934	303.15	6000.00	-5.857
0.6934	308.15	6000.00	-5.941
0.6947	308.15	6500.00	-5.547
0.6958	308.15	7000.00	-5.077
0.6969	308.15	7500.00	-4.364
0.7317	298.15	5000.00	-6.796
0.7317	303.15	5000.00	-6.849
0.7331	298.15	5500.00	-6.375
0.7331	303.15	5500.00	-6.529
0.7331	308.15	5500.00	-6.576
0.7344	298.15	6000.00	-5.583
0.7344	303.15	6000.00	-6.174
0.7344	308.15	6000.00	-6.23
0.7355	308.15	6500.00	-5.804
0.7366	308.15	7000.00	-5.288
0.7376	308.15	7500.00	-4.613
0.7692	298.15	5000.00	-7.156
0.7705	298.15	5500.00	-6.747
0.7705	303.15	5500.00	-6.845
0.7716	298.15	6000.00	-5.843
0.7716	303.15	6000.00	-6.449
0.7716	308.15	6000.00	-6.528
0.7727	308.15	6500.00	-6.056
0.7736	308.15	7000.00	-5.562
0.7745	308.15	7500.00	-4.798
0.8036	298.15	5000.00	-7.495
0.8047	298.15	5500.00	-6.996
0.8047	303.15	5500.00	-7.083
0.8057	298.15	6000.00	-6.172
0.8057	303.15	6000.00	-6.703
0.8057	308.15	6000.00	-6.728
0.8066	308.15	6500.00	-6.267
0.8075	308.15	7000.00	-5.776
0.8083	308.15	7500.00	-4.971
0.8248	308.15	6000.00	-6.851
0.8351	298.15	5000.00	-7.726
0.8361	298.15	5500.00	-7.264
0.8370	298.15	6000.00	-6.37
0.8370	303.15	6000.00	-6.956
0.8378	308.15	6500.00	-6.522
0.8385	308.15	7000.00	-5.928
0.8392	308.15	7500.00	-5.178
0.8650	298.15	5500.00	-7.436
0.8658	298.15	6000.00	-6.637
0.8658	303.15	6000.00	-7.126
0.8665	308.15	6500.00	-6.705
0.8671	308.15	7000.00	-6.02
0.8677	308.15	7500.00	-5.25
0.8918	298.15	5500.00	-7.621
0.8924	298.15	6000.00	-6.806
0.8924	303.15	6000.00	-7.157
0.8935	308.15	7000.00	-6.098
0.8940	308.15	7500.00	-5.358
0.9019	298.15	5500.00	-7.673
0.9171	298.15	6000.00	-6.921
0.9179	308.15	7000.00	-6.144
0.9183	308.15	7500.00	-5.251
0.9310	298.15	6000.00	-6.837
0.9400	298.15	6000.00	-6.969
0.9409	308.15	7500.00	-5.174
0.9614	298.15	6000.00	-6.872
0.9620	308.15	7500.00	-4.909
0.9813	298.15	6000.00	-6.209

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1127	293.15	560.00
0.1154	333.15	741.00
0.1235	313.15	661.00
0.1728	333.15	1104.00
0.1831	273.15	547.00
0.1946	313.15	1116.00
0.2281	293.15	1185.00
0.2668	333.15	1672.00
0.2728	313.15	1542.00
0.2795	265.15	682.00
0.2961	293.15	1537.00
0.3091	273.15	983.00
0.3447	333.15	2181.00
0.3666	313.15	2135.00
0.3754	265.15	1049.00
0.3828	333.15	2554.00
0.4015	293.15	2051.00
0.4024	313.15	2490.00
0.4361	273.15	1471.00
0.4907	293.15	2551.00
0.5112	265.15	1505.00
0.5756	273.15	2031.00
0.6450	273.15	2526.00
0.6565	265.15	2021.00
0.7589	265.15	2478.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1127	293.15	560.00
0.1154	333.15	741.00
0.1235	313.15	661.00
0.1728	333.15	1104.00
0.1831	273.15	547.00
0.1946	313.15	1116.00
0.2281	293.15	1185.00
0.2668	333.15	1672.00
0.2728	313.15	1542.00
0.2795	265.15	682.00
0.2961	293.15	1537.00
0.3091	273.15	983.00
0.3447	333.15	2181.00
0.3666	313.15	2135.00
0.3754	265.15	1049.00
0.3828	333.15	2554.00
0.4015	293.15	2051.00
0.4024	313.15	2490.00
0.4361	273.15	1471.00
0.4907	293.15	2551.00
0.5112	265.15	1505.00
0.5756	273.15	2031.00
0.6450	273.15	2526.00
0.6565	265.15	2021.00
0.7589	265.15	2478.00

Sources

• Measurement and correlation of vapor liquid equilibria for the system carbon dioxide diisopropyl ether
• Determination and Correlation of Excess Molar Enthalpies of the Binary Carbon Dioxide + Diisopropyl Ether (DIPE) System at Temperatures from (298.15 to 308.15) K and Pressures from (5.0 to 7.5) MPa