Mixture of Toluene + Carbon dioxide

Datasets

1. Mole fraction (14)
2. P_c - Critical pressure, kPa (2)
3. P_vap - Vapor or sublimation pressure, kPa (16)
4. ρ_l - Mass density, kg/m3 (2)
5. ρ_m,l - Amount density, mol/m3 (2)
6. T_boil - Boiling temperature at pressure P, K (2)
7. T_c - Critical temperature, K (2)
8. Binary diffusion coefficient, m2/s (2)
9. Vapor or sublimation pressure, kPa (6)
10. V_m - Molar volume, m3/mol (2)

Mole fraction of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 352.6 (Liquid)

Pressure, kPa - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
160.00	0.0049
400.00	0.0186
970.00	0.0480
1200.00	0.0640
1460.00	0.0785
1760.00	0.0994
2090.00	0.1189
2360.00	0.1337
2980.00	0.1672

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Gas	Mole fraction of Carbon dioxide (2) - Gas
0.0357	353.15	0.9048
0.0397	353.15	0.8980
0.0449	311.15	0.9806
0.0578	283.15	0.9947
0.0715	353.15	0.9562
0.0932	353.15	0.9630
0.0986	391.45	0.9285
0.1104	353.15	0.9726
0.1105	311.15	0.9902
0.1215	353.15	0.9749
0.1274	283.15	0.9948
0.1381	391.45	0.9462
0.1928	283.15	0.9951
0.1939	353.15	0.9817
0.1997	311.15	0.9935
0.2045	353.15	0.9755
0.2382	391.45	0.9541
0.2450	353.15	0.9849
0.2476	311.15	0.9912
0.2511	283.15	0.9964
0.2867	311.15	0.9955
0.2935	353.15	0.9841
0.2946	353.15	0.9850
0.3213	391.45	0.9536
0.3287	353.15	0.9889
0.3709	283.15	0.9968
0.3816	353.15	0.9845
0.3997	391.45	0.9485
0.4067	311.15	0.9927
0.4335	391.45	0.9484
0.4484	353.15	0.9836
0.4972	353.15	0.9828
0.5249	283.15	0.9981
0.5335	311.15	0.9941
0.5467	391.45	0.9325
0.5665	311.15	0.9945
0.6816	353.15	0.9697
0.6986	311.15	0.9945
0.6988	283.15	0.9989
0.7613	311.15	0.9936
0.7848	311.15	0.9939
0.7980	283.15	0.9990
0.8871	311.15	0.9939

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
0.0784	343.10	0.9695
0.1570	343.00	0.9805
0.2350	343.00	0.9837
0.2940	343.10	0.9876
0.3720	343.10	0.9881
0.1370	313.00	0.9921
0.2160	313.10	0.9940
0.3140	313.10	0.9956
0.4115	313.00	0.9962
0.4711	313.00	0.9964

Mole fraction of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 352.6 (Liquid)

Pressure, kPa - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
280.00	0.0118
690.00	0.0333
1090.00	0.0560
1610.00	0.0890
1930.00	0.1092
2670.00	0.1505
3030.00	0.1696

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
1700.00	293.15	0.2500
1700.00	298.15	0.2380
1700.00	308.15	0.2170
2210.00	293.15	0.3290
2210.00	298.15	0.3010
2210.00	308.15	0.2800
2720.00	293.15	0.4210
2720.00	298.15	0.3730
2720.00	308.15	0.3320
3230.00	293.15	0.5030
3230.00	298.15	0.4540
3230.00	308.15	0.4010
3740.00	293.15	0.5860
3740.00	298.15	0.5430
3740.00	308.15	0.4750
4250.00	293.15	0.7110
4250.00	298.15	0.6190
4250.00	308.15	0.5290
4760.00	293.15	0.8820
4760.00	298.15	0.7750
4760.00	308.15	0.5940
5270.00	293.15	0.9450
5270.00	298.15	0.8550
5270.00	308.15	0.7110
5780.00	298.15	0.9630
5780.00	308.15	0.7950
6290.00	308.15	0.8870
6800.00	308.15	0.9150
7310.00	308.15	0.9710

Mole fraction of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 323.2 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Carbon dioxide (2) - Gas
0.1330	0.9860
0.2160	0.9910
0.2470	0.9920
0.3000	0.9920
0.3210	0.9920
0.3870	0.9910
0.4910	0.9890
0.5670	0.9860
0.7360	0.9830
0.8920	0.9820

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
298.15	930.00	0.1060
298.15	1590.00	0.1950
298.15	2270.00	0.3040
298.15	2960.00	0.4150
298.15	3650.00	0.5370
298.15	4340.00	0.6570
298.15	5070.00	0.7550
308.15	1000.00	0.0960
308.15	1670.00	0.1780
308.15	2380.00	0.2580
308.15	3070.00	0.3440
308.15	3760.00	0.4210
308.15	4450.00	0.4980
308.15	5070.00	0.5580
338.15	930.00	0.0630
338.15	1620.00	0.1090
338.15	2310.00	0.1620
338.15	3000.00	0.2120
338.15	3690.00	0.2610
338.15	4310.00	0.3100
338.15	5070.00	0.3670
363.15	930.00	0.0410
363.15	1620.00	0.0820
363.15	2310.00	0.1190
363.15	3000.00	0.1550
363.15	3670.00	0.1920
363.15	4380.00	0.2330
363.15	4930.00	0.2620

Mole fraction of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 352.6 (Liquid)

Pressure, kPa - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
160.00	0.0049
400.00	0.0186
970.00	0.0480
1200.00	0.0640
1460.00	0.0785
1760.00	0.0994
2090.00	0.1189
2360.00	0.1337
2980.00	0.1672

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Gas	Mole fraction of Carbon dioxide (2) - Gas
0.0357	353.15	0.9048
0.0397	353.15	0.8980
0.0449	311.15	0.9806
0.0578	283.15	0.9947
0.0715	353.15	0.9562
0.0932	353.15	0.9630
0.0986	391.45	0.9285
0.1104	353.15	0.9726
0.1105	311.15	0.9902
0.1215	353.15	0.9749
0.1274	283.15	0.9948
0.1381	391.45	0.9462
0.1928	283.15	0.9951
0.1939	353.15	0.9817
0.1997	311.15	0.9935
0.2045	353.15	0.9755
0.2382	391.45	0.9541
0.2450	353.15	0.9849
0.2476	311.15	0.9912
0.2511	283.15	0.9964
0.2867	311.15	0.9955
0.2935	353.15	0.9841
0.2946	353.15	0.9850
0.3213	391.45	0.9536
0.3287	353.15	0.9889
0.3709	283.15	0.9968
0.3816	353.15	0.9845
0.3997	391.45	0.9485
0.4067	311.15	0.9927
0.4335	391.45	0.9484
0.4484	353.15	0.9836
0.4972	353.15	0.9828
0.5249	283.15	0.9981
0.5335	311.15	0.9941
0.5467	391.45	0.9325
0.5665	311.15	0.9945
0.6816	353.15	0.9697
0.6986	311.15	0.9945
0.6988	283.15	0.9989
0.7613	311.15	0.9936
0.7848	311.15	0.9939
0.7980	283.15	0.9990
0.8871	311.15	0.9939

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
0.0784	343.10	0.9695
0.1570	343.00	0.9805
0.2350	343.00	0.9837
0.2940	343.10	0.9876
0.3720	343.10	0.9881
0.1370	313.00	0.9921
0.2160	313.10	0.9940
0.3140	313.10	0.9956
0.4115	313.00	0.9962
0.4711	313.00	0.9964

Mole fraction of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 352.6 (Liquid)

Pressure, kPa - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
280.00	0.0118
690.00	0.0333
1090.00	0.0560
1610.00	0.0890
1930.00	0.1092
2670.00	0.1505
3030.00	0.1696

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
1700.00	293.15	0.2500
1700.00	298.15	0.2380
1700.00	308.15	0.2170
2210.00	293.15	0.3290
2210.00	298.15	0.3010
2210.00	308.15	0.2800
2720.00	293.15	0.4210
2720.00	298.15	0.3730
2720.00	308.15	0.3320
3230.00	293.15	0.5030
3230.00	298.15	0.4540
3230.00	308.15	0.4010
3740.00	293.15	0.5860
3740.00	298.15	0.5430
3740.00	308.15	0.4750
4250.00	293.15	0.7110
4250.00	298.15	0.6190
4250.00	308.15	0.5290
4760.00	293.15	0.8820
4760.00	298.15	0.7750
4760.00	308.15	0.5940
5270.00	293.15	0.9450
5270.00	298.15	0.8550
5270.00	308.15	0.7110
5780.00	298.15	0.9630
5780.00	308.15	0.7950
6290.00	308.15	0.8870
6800.00	308.15	0.9150
7310.00	308.15	0.9710

Mole fraction of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 323.2 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Carbon dioxide (2) - Gas
0.1330	0.9860
0.2160	0.9910
0.2470	0.9920
0.3000	0.9920
0.3210	0.9920
0.3870	0.9910
0.4910	0.9890
0.5670	0.9860
0.7360	0.9830
0.8920	0.9820

Mole fraction of Carbon dioxide (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
298.15	930.00	0.1060
298.15	1590.00	0.1950
298.15	2270.00	0.3040
298.15	2960.00	0.4150
298.15	3650.00	0.5370
298.15	4340.00	0.6570
298.15	5070.00	0.7550
308.15	1000.00	0.0960
308.15	1670.00	0.1780
308.15	2380.00	0.2580
308.15	3070.00	0.3440
308.15	3760.00	0.4210
308.15	4450.00	0.4980
308.15	5070.00	0.5580
338.15	930.00	0.0630
338.15	1620.00	0.1090
338.15	2310.00	0.1620
338.15	3000.00	0.2120
338.15	3690.00	0.2610
338.15	4310.00	0.3100
338.15	5070.00	0.3670
363.15	930.00	0.0410
363.15	1620.00	0.0820
363.15	2310.00	0.1190
363.15	3000.00	0.1550
363.15	3670.00	0.1920
363.15	4380.00	0.2330
363.15	4930.00	0.2620

Critical pressure, kPa [ref]

Mole fraction of Toluene (1) - Liquid	Critical pressure, kPa - Liquid
0.1000	10160.00
0.2000	15510.00

Critical pressure, kPa [ref]

Mole fraction of Toluene (1) - Liquid	Critical pressure, kPa - Liquid
0.1000	10160.00
0.2000	15510.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0784	343.10	1120.00
0.1570	343.00	2205.00
0.2350	343.00	3351.00
0.2940	343.10	4211.00
0.3720	343.10	5420.00
0.1370	313.00	1375.00
0.2160	313.10	2172.00
0.3140	313.10	3173.00
0.4115	313.00	4162.00
0.4711	313.00	4651.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
312.80	0.2346	2516.00
313.10	0.2452	2596.00
313.00	0.4773	4671.00
313.00	0.5336	4970.00
313.00	0.5545	5103.00
313.10	0.5678	5211.00
313.00	0.5741	5321.00
313.00	0.5823	5332.00
313.10	0.5983	5438.00
313.10	0.6660	5790.00
313.00	0.6791	5917.00
313.10	0.6927	5990.00
313.00	0.7069	6121.00
313.00	0.7217	6200.00
313.10	0.7371	6316.00
313.00	0.7623	6420.00
342.90	0.2412	3473.00
342.90	0.2473	3560.00
343.10	0.2556	3787.00
343.10	0.2645	3936.00
343.00	0.2740	4106.00
343.00	0.2841	4240.00
343.10	0.4853	7142.00
343.00	0.4986	7426.00
343.10	0.5126	7614.00
343.00	0.5275	7797.00
343.00	0.5432	7987.00
343.10	0.7650	10180.00
343.10	0.7871	10331.00
343.00	0.8038	10509.00
343.00	0.8196	10705.00
343.00	0.8396	10926.00
343.00	0.8588	11117.00
343.10	0.8788	11305.00
343.10	0.8997	11418.00
343.00	0.9217	11474.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Mole fraction = 0.9211 (Liquid)

Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.56	6399.00
312.39	7525.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0910	1200.00
0.1750	2120.00
0.2600	3150.00
0.3350	4010.00
0.4080	4810.00
0.4800	5540.00
0.5240	5960.00
0.5830	6310.00
0.6440	6720.00
0.7150	7380.00
0.7640	7800.00
0.8210	8210.00
0.8650	8500.00
0.8830	8660.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.20	0.2000	9470.00
333.20	0.3000	8830.00
333.20	0.4000	8090.00
333.20	0.5000	6790.00
343.20	0.2000	10930.00
343.20	0.3000	10050.00
343.20	0.4000	8910.00
353.20	0.2000	12030.00
353.20	0.3000	11280.00
353.20	0.4000	10160.00
353.20	0.5000	8480.00
353.20	0.6000	6990.00
363.20	0.2000	13180.00
363.20	0.3000	12420.00
363.20	0.4000	11200.00
373.20	0.2000	14110.00
373.20	0.3000	13620.00
373.20	0.4000	12120.00
373.20	0.5000	9980.00
373.20	0.6000	8200.00
383.20	0.2000	14860.00
383.20	0.3000	14550.00
383.20	0.4000	13140.00
393.20	0.3000	15280.00
393.20	0.4000	13970.00
393.20	0.5000	11410.00
393.20	0.6000	9470.00
393.20	0.7000	7360.00
403.20	0.3000	15960.00
403.20	0.4000	14810.00
413.20	0.3000	16300.00
413.20	0.4000	15460.00
413.20	0.5000	12720.00
413.20	0.6000	10350.00
413.20	0.7000	8010.00
423.20	0.3000	16490.00
423.20	0.4000	15920.00
433.20	0.4000	16190.00
433.20	0.5000	13840.00
433.20	0.6000	11290.00
433.20	0.7000	8850.00
443.20	0.4000	16350.00
453.20	0.4000	16350.00
453.20	0.5000	15120.00
453.20	0.6000	11930.00
453.20	0.7000	9490.00
463.20	0.4000	16080.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
473.20	0.5000	15220.00
473.20	0.6000	12400.00
473.20	0.7000	10010.00
485.00	0.5000	14940.00
493.00	0.6000	12800.00
493.00	0.7000	10210.00
493.00	0.8000	6830.00
503.00	0.6000	12750.00
513.00	0.6000	12480.00
513.00	0.7000	10390.00
513.00	0.8000	7470.00
523.00	0.6000	12010.00
533.00	0.6000	11190.00
533.00	0.7000	10310.00
533.00	0.8000	7620.00
553.00	0.8000	7670.00
565.00	0.8000	7200.00
572.00	0.8000	6740.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.2 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1330	1870.00
0.2160	2870.00
0.2470	3450.00
0.3000	4250.00
0.3210	4270.00
0.3870	4940.00
0.4910	5800.00
0.5670	6620.00
0.7360	7990.00
0.8920	8720.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.5020	293.15	3680.00
0.5020	298.15	3800.00
0.5020	303.15	4210.00
0.5020	308.15	4500.00
0.5020	313.15	4920.00
0.6010	293.15	4060.00
0.6010	298.15	4530.00
0.6010	303.15	4880.00
0.6010	308.15	5400.00
0.6010	313.15	5820.00
0.7070	293.15	4420.00
0.7070	298.15	5030.00
0.7070	303.15	5460.00
0.7070	308.15	6010.00
0.7070	313.15	6510.00
0.8080	293.15	4810.00
0.8080	298.15	5300.00
0.8080	303.15	5950.00
0.8080	308.15	6390.00
0.8080	313.15	7050.00
0.9030	293.15	4930.00
0.9030	298.15	5580.00
0.9030	303.15	6290.00
0.9030	308.15	6910.00
0.9030	313.15	7490.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0784	343.10	1120.00
0.1570	343.00	2205.00
0.2350	343.00	3351.00
0.2940	343.10	4211.00
0.3720	343.10	5420.00
0.1370	313.00	1375.00
0.2160	313.10	2172.00
0.3140	313.10	3173.00
0.4115	313.00	4162.00
0.4711	313.00	4651.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
312.80	0.2346	2516.00
313.10	0.2452	2596.00
313.00	0.4773	4671.00
313.00	0.5336	4970.00
313.00	0.5545	5103.00
313.10	0.5678	5211.00
313.00	0.5741	5321.00
313.00	0.5823	5332.00
313.10	0.5983	5438.00
313.10	0.6660	5790.00
313.00	0.6791	5917.00
313.10	0.6927	5990.00
313.00	0.7069	6121.00
313.00	0.7217	6200.00
313.10	0.7371	6316.00
313.00	0.7623	6420.00
342.90	0.2412	3473.00
342.90	0.2473	3560.00
343.10	0.2556	3787.00
343.10	0.2645	3936.00
343.00	0.2740	4106.00
343.00	0.2841	4240.00
343.10	0.4853	7142.00
343.00	0.4986	7426.00
343.10	0.5126	7614.00
343.00	0.5275	7797.00
343.00	0.5432	7987.00
343.10	0.7650	10180.00
343.10	0.7871	10331.00
343.00	0.8038	10509.00
343.00	0.8196	10705.00
343.00	0.8396	10926.00
343.00	0.8588	11117.00
343.10	0.8788	11305.00
343.10	0.8997	11418.00
343.00	0.9217	11474.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Mole fraction = 0.9211 (Liquid)

Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.56	6399.00
312.39	7525.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0910	1200.00
0.1750	2120.00
0.2600	3150.00
0.3350	4010.00
0.4080	4810.00
0.4800	5540.00
0.5240	5960.00
0.5830	6310.00
0.6440	6720.00
0.7150	7380.00
0.7640	7800.00
0.8210	8210.00
0.8650	8500.00
0.8830	8660.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.20	0.2000	9470.00
333.20	0.3000	8830.00
333.20	0.4000	8090.00
333.20	0.5000	6790.00
343.20	0.2000	10930.00
343.20	0.3000	10050.00
343.20	0.4000	8910.00
353.20	0.2000	12030.00
353.20	0.3000	11280.00
353.20	0.4000	10160.00
353.20	0.5000	8480.00
353.20	0.6000	6990.00
363.20	0.2000	13180.00
363.20	0.3000	12420.00
363.20	0.4000	11200.00
373.20	0.2000	14110.00
373.20	0.3000	13620.00
373.20	0.4000	12120.00
373.20	0.5000	9980.00
373.20	0.6000	8200.00
383.20	0.2000	14860.00
383.20	0.3000	14550.00
383.20	0.4000	13140.00
393.20	0.3000	15280.00
393.20	0.4000	13970.00
393.20	0.5000	11410.00
393.20	0.6000	9470.00
393.20	0.7000	7360.00
403.20	0.3000	15960.00
403.20	0.4000	14810.00
413.20	0.3000	16300.00
413.20	0.4000	15460.00
413.20	0.5000	12720.00
413.20	0.6000	10350.00
413.20	0.7000	8010.00
423.20	0.3000	16490.00
423.20	0.4000	15920.00
433.20	0.4000	16190.00
433.20	0.5000	13840.00
433.20	0.6000	11290.00
433.20	0.7000	8850.00
443.20	0.4000	16350.00
453.20	0.4000	16350.00
453.20	0.5000	15120.00
453.20	0.6000	11930.00
453.20	0.7000	9490.00
463.20	0.4000	16080.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
473.20	0.5000	15220.00
473.20	0.6000	12400.00
473.20	0.7000	10010.00
485.00	0.5000	14940.00
493.00	0.6000	12800.00
493.00	0.7000	10210.00
493.00	0.8000	6830.00
503.00	0.6000	12750.00
513.00	0.6000	12480.00
513.00	0.7000	10390.00
513.00	0.8000	7470.00
523.00	0.6000	12010.00
533.00	0.6000	11190.00
533.00	0.7000	10310.00
533.00	0.8000	7620.00
553.00	0.8000	7670.00
565.00	0.8000	7200.00
572.00	0.8000	6740.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.2 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1330	1870.00
0.2160	2870.00
0.2470	3450.00
0.3000	4250.00
0.3210	4270.00
0.3870	4940.00
0.4910	5800.00
0.5670	6620.00
0.7360	7990.00
0.8920	8720.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.5020	293.15	3680.00
0.5020	298.15	3800.00
0.5020	303.15	4210.00
0.5020	308.15	4500.00
0.5020	313.15	4920.00
0.6010	293.15	4060.00
0.6010	298.15	4530.00
0.6010	303.15	4880.00
0.6010	308.15	5400.00
0.6010	313.15	5820.00
0.7070	293.15	4420.00
0.7070	298.15	5030.00
0.7070	303.15	5460.00
0.7070	308.15	6010.00
0.7070	313.15	6510.00
0.8080	293.15	4810.00
0.8080	298.15	5300.00
0.8080	303.15	5950.00
0.8080	308.15	6390.00
0.8080	313.15	7050.00
0.9030	293.15	4930.00
0.9030	298.15	5580.00
0.9030	303.15	6290.00
0.9030	308.15	6910.00
0.9030	313.15	7490.00

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	930.00	867.2
298.15	1590.00	871.1
298.15	2270.00	875.7
298.15	2960.00	880.6
298.15	3650.00	885.8
298.15	4340.00	887.0
298.15	5070.00	885.3
308.15	1000.00	857.0
308.15	1670.00	859.8
308.15	2380.00	862.7
308.15	3070.00	865.7
308.15	3760.00	868.3
308.15	4450.00	871.0
308.15	5070.00	871.3
338.15	930.00	826.6
338.15	1620.00	827.8
338.15	2310.00	828.6
338.15	3000.00	829.4
338.15	3690.00	830.4
338.15	4310.00	831.3
338.15	5070.00	831.2
363.15	930.00	801.3
363.15	1620.00	801.4
363.15	2310.00	801.6
363.15	3000.00	801.8
363.15	3670.00	801.6
363.15	4380.00	801.3
363.15	4930.00	801.4

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	930.00	867.2
298.15	1590.00	871.1
298.15	2270.00	875.7
298.15	2960.00	880.6
298.15	3650.00	885.8
298.15	4340.00	887.0
298.15	5070.00	885.3
308.15	1000.00	857.0
308.15	1670.00	859.8
308.15	2380.00	862.7
308.15	3070.00	865.7
308.15	3760.00	868.3
308.15	4450.00	871.0
308.15	5070.00	871.3
338.15	930.00	826.6
338.15	1620.00	827.8
338.15	2310.00	828.6
338.15	3000.00	829.4
338.15	3690.00	830.4
338.15	4310.00	831.3
338.15	5070.00	831.2
363.15	930.00	801.3
363.15	1620.00	801.4
363.15	2310.00	801.6
363.15	3000.00	801.8
363.15	3670.00	801.6
363.15	4380.00	801.3
363.15	4930.00	801.4

Amount density, mol/m3 [ref]

Operational condition: Mole fraction = 0.9 (Fluid (supercritical or subcritical phases))

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Amount density, mol/m3 - Fluid (supercritical or subcritical phases)
313.20	4400.00	2980.0
313.20	6760.00	6700.0
313.20	7190.00	8440.0
313.20	7540.00	10140.0
313.20	7850.00	12250.0
313.20	8040.00	13750.0
313.20	8530.00	15770.0
323.20	4740.00	2980.0
323.20	7780.00	6700.0
323.20	8540.00	8440.0
323.20	8950.00	10140.0
323.20	9420.00	12250.0
323.20	9760.00	13750.0
323.20	11000.00	15770.0
333.20	5070.00	2980.0
333.20	8710.00	6700.0
333.20	9690.00	8440.0
333.20	10290.00	10140.0
333.20	10960.00	12250.0
333.20	11600.00	13750.0
333.20	15350.00	15770.0
343.20	5410.00	2980.0
343.20	9550.00	6700.0
343.20	10730.00	8440.0
343.20	11590.00	10140.0
343.20	12630.00	12250.0
343.20	13680.00	13750.0
343.20	19790.00	15770.0
353.20	5740.00	2980.0
353.20	10360.00	6700.0
353.20	11830.00	8440.0
353.20	12850.00	10140.0
353.20	14260.00	12250.0
353.20	16660.00	13750.0
353.20	24390.00	15770.0
363.20	6060.00	2980.0
363.20	11190.00	6700.0
363.20	12830.00	8440.0
363.20	14080.00	10140.0
363.20	16380.00	12250.0
363.20	19780.00	13750.0
363.20	28990.00	15770.0
373.20	6390.00	2980.0
373.20	11970.00	6700.0
373.20	13810.00	8440.0
373.20	15330.00	10140.0
373.20	18810.00	12250.0
373.20	23110.00	13750.0
373.20	33580.00	15770.0
383.20	6770.00	2980.0
383.20	12740.00	6700.0
383.20	14880.00	8440.0
383.20	16890.00	10140.0
383.20	21340.00	12250.0
383.20	26440.00	13750.0
383.20	38330.00	15770.0
393.20	7110.00	2980.0
393.20	13500.00	6700.0
393.20	15990.00	8440.0
393.20	18670.00	10140.0
393.20	24000.00	12250.0
393.20	29820.00	13750.0
393.20	43060.00	15770.0

Amount density, mol/m3 [ref]

Operational condition: Mole fraction = 0.9 (Fluid (supercritical or subcritical phases))

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Amount density, mol/m3 - Fluid (supercritical or subcritical phases)
313.20	4400.00	2980.0
313.20	6760.00	6700.0
313.20	7190.00	8440.0
313.20	7540.00	10140.0
313.20	7850.00	12250.0
313.20	8040.00	13750.0
313.20	8530.00	15770.0
323.20	4740.00	2980.0
323.20	7780.00	6700.0
323.20	8540.00	8440.0
323.20	8950.00	10140.0
323.20	9420.00	12250.0
323.20	9760.00	13750.0
323.20	11000.00	15770.0
333.20	5070.00	2980.0
333.20	8710.00	6700.0
333.20	9690.00	8440.0
333.20	10290.00	10140.0
333.20	10960.00	12250.0
333.20	11600.00	13750.0
333.20	15350.00	15770.0
343.20	5410.00	2980.0
343.20	9550.00	6700.0
343.20	10730.00	8440.0
343.20	11590.00	10140.0
343.20	12630.00	12250.0
343.20	13680.00	13750.0
343.20	19790.00	15770.0
353.20	5740.00	2980.0
353.20	10360.00	6700.0
353.20	11830.00	8440.0
353.20	12850.00	10140.0
353.20	14260.00	12250.0
353.20	16660.00	13750.0
353.20	24390.00	15770.0
363.20	6060.00	2980.0
363.20	11190.00	6700.0
363.20	12830.00	8440.0
363.20	14080.00	10140.0
363.20	16380.00	12250.0
363.20	19780.00	13750.0
363.20	28990.00	15770.0
373.20	6390.00	2980.0
373.20	11970.00	6700.0
373.20	13810.00	8440.0
373.20	15330.00	10140.0
373.20	18810.00	12250.0
373.20	23110.00	13750.0
373.20	33580.00	15770.0
383.20	6770.00	2980.0
383.20	12740.00	6700.0
383.20	14880.00	8440.0
383.20	16890.00	10140.0
383.20	21340.00	12250.0
383.20	26440.00	13750.0
383.20	38330.00	15770.0
393.20	7110.00	2980.0
393.20	13500.00	6700.0
393.20	15990.00	8440.0
393.20	18670.00	10140.0
393.20	24000.00	12250.0
393.20	29820.00	13750.0
393.20	43060.00	15770.0

Boiling temperature at pressure P, K [ref]

Operational condition: Mole fraction = 0.9 (Gas)

Pressure, kPa - Gas	Boiling temperature at pressure P, K - Gas
11100.00	323.60
13000.00	341.20
14900.00	357.00
15200.00	386.00
15500.00	374.40

Boiling temperature at pressure P, K [ref]

Operational condition: Mole fraction = 0.9 (Gas)

Pressure, kPa - Gas	Boiling temperature at pressure P, K - Gas
11100.00	323.60
13000.00	341.20
14900.00	357.00
15200.00	386.00
15500.00	374.40

Critical temperature, K [ref]

Mole fraction of Toluene (1) - Liquid	Critical temperature, K - Liquid
0.1000	333.20
0.2000	393.20

Critical temperature, K [ref]

Mole fraction of Toluene (1) - Liquid	Critical temperature, K - Liquid
0.1000	333.20
0.2000	393.20

Binary diffusion coefficient, m2/s [ref]

Operational condition: Mole fraction = 0 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Binary diffusion coefficient, m2/s - Liquid
298.00	1000.00	0.0000
298.00	11000.00	0.0000
298.00	30000.00	0.0000
298.00	48000.00	0.0000
298.00	68000.00	0.0000
323.00	1000.00	0.0000
323.00	10000.00	0.0000
323.00	30000.00	0.0000
323.00	49000.00	0.0000
323.00	66000.00	0.0000
348.00	1000.00	0.0000
348.00	11000.00	0.0000
348.00	30000.00	0.0000
348.00	48000.00	0.0000
348.00	67000.00	0.0000
373.00	1000.00	1.1400e-08
373.00	10000.00	1.0400e-08
373.00	30000.00	0.0000
373.00	51000.00	0.0000
373.00	67000.00	0.0000
398.00	1000.00	1.3800e-08
398.00	10000.00	1.2400e-08
398.00	30000.00	1.1700e-08
398.00	48000.00	1.0500e-08
398.00	68000.00	0.0000
423.00	1100.00	1.6000e-08
423.00	10000.00	1.5000e-08
423.00	30000.00	1.4000e-08
423.00	50000.00	1.2300e-08
423.00	67000.00	1.1400e-08

Binary diffusion coefficient, m2/s [ref]

Operational condition: Mole fraction = 0 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Binary diffusion coefficient, m2/s - Liquid
298.00	1000.00	0.0000
298.00	11000.00	0.0000
298.00	30000.00	0.0000
298.00	48000.00	0.0000
298.00	68000.00	0.0000
323.00	1000.00	0.0000
323.00	10000.00	0.0000
323.00	30000.00	0.0000
323.00	49000.00	0.0000
323.00	66000.00	0.0000
348.00	1000.00	0.0000
348.00	11000.00	0.0000
348.00	30000.00	0.0000
348.00	48000.00	0.0000
348.00	67000.00	0.0000
373.00	1000.00	1.1400e-08
373.00	10000.00	1.0400e-08
373.00	30000.00	0.0000
373.00	51000.00	0.0000
373.00	67000.00	0.0000
398.00	1000.00	1.3800e-08
398.00	10000.00	1.2400e-08
398.00	30000.00	1.1700e-08
398.00	48000.00	1.0500e-08
398.00	68000.00	0.0000
423.00	1100.00	1.6000e-08
423.00	10000.00	1.5000e-08
423.00	30000.00	1.4000e-08
423.00	50000.00	1.2300e-08
423.00	67000.00	1.1400e-08

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0357	353.15	589.00
0.0397	353.15	541.00
0.0449	311.15	552.00
0.0578	283.15	405.00
0.0715	353.15	1252.00
0.0932	353.15	1679.00
0.0986	391.45	2064.00
0.1104	353.15	2012.00
0.1105	311.15	1144.00
0.1215	353.15	2138.00
0.1274	283.15	878.00
0.1381	391.45	3390.00
0.1928	283.15	1277.00
0.1939	353.15	3255.00
0.1997	311.15	2039.00
0.2045	353.15	3563.00
0.2382	391.45	5240.00
0.2450	353.15	4207.00
0.2476	311.15	2534.00
0.2511	283.15	1624.00
0.2867	311.15	3133.00
0.2935	353.15	5158.00
0.2946	353.15	5257.00
0.3213	391.45	7429.00
0.3287	353.15	5823.00
0.3709	283.15	2223.00
0.3816	353.15	6569.00
0.3997	391.45	9439.00
0.4067	311.15	3968.00
0.4335	391.45	10014.00
0.4484	353.15	7815.00
0.4972	353.15	8435.00
0.5249	283.15	2940.00
0.5335	311.15	5014.00
0.5467	391.45	12133.00
0.5665	311.15	5225.00
0.6816	353.15	10649.00
0.6986	311.15	6064.00
0.6988	283.15	3532.00
0.7613	311.15	6429.00
0.7848	311.15	6644.00
0.7980	283.15	3783.00
0.8871	311.15	7191.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Toluene (1) - Gas	Vapor or sublimation pressure, kPa - Gas
343.20	0.1000	11270.00
353.20	0.1000	12290.00
363.20	0.1000	13110.00
373.20	0.1000	13740.00
383.20	0.1000	13980.00
393.20	0.1000	13980.00
403.20	0.1000	13570.00
403.20	0.2000	15860.00
413.20	0.2000	15990.00
420.50	0.1000	12430.00
423.20	0.2000	15990.00
424.50	0.1000	10600.00
425.30	0.1000	6770.00
426.80	0.1000	7670.00
427.40	0.1000	8620.00
433.20	0.2000	15710.00
433.20	0.3000	16580.00
443.20	0.2000	15070.00
443.20	0.3000	16490.00
451.00	0.2000	14340.00
453.20	0.3000	16340.00
463.20	0.3000	15820.00
466.80	0.2000	6790.00
468.70	0.2000	12420.00
472.20	0.2000	10650.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Toluene (1) - Gas	Vapor or sublimation pressure, kPa - Gas
473.20	0.2000	8620.00
473.20	0.3000	15100.00
473.20	0.4000	15690.00
483.00	0.3000	13880.00
483.00	0.4000	15170.00
493.00	0.4000	14400.00
493.00	0.5000	14570.00
494.00	0.3000	12460.00
496.00	0.3000	6770.00
497.00	0.3000	11540.00
499.00	0.3000	7690.00
499.00	0.5000	14090.00
501.00	0.3000	10600.00
502.00	0.3000	9670.00
502.00	0.3000	8620.00
504.00	0.4000	13370.00
510.00	0.4000	12440.00
516.00	0.4000	6790.00
520.00	0.5000	12470.00
521.00	0.4000	10600.00
522.00	0.4000	8650.00
534.00	0.5000	10620.00
535.00	0.5000	6770.00
539.00	0.5000	8620.00
548.00	0.6000	9640.00
550.00	0.6000	6770.00
552.00	0.6000	8620.00
553.00	0.7000	9020.00
557.00	0.7000	8600.00
563.00	0.7000	7690.00
564.00	0.7000	6770.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Gas
0.0357	353.15	589.00
0.0397	353.15	541.00
0.0449	311.15	552.00
0.0578	283.15	405.00
0.0715	353.15	1252.00
0.0932	353.15	1679.00
0.0986	391.45	2064.00
0.1104	353.15	2012.00
0.1105	311.15	1144.00
0.1215	353.15	2138.00
0.1274	283.15	878.00
0.1381	391.45	3390.00
0.1928	283.15	1277.00
0.1939	353.15	3255.00
0.1997	311.15	2039.00
0.2045	353.15	3563.00
0.2382	391.45	5240.00
0.2450	353.15	4207.00
0.2476	311.15	2534.00
0.2511	283.15	1624.00
0.2867	311.15	3133.00
0.2935	353.15	5158.00
0.2946	353.15	5257.00
0.3213	391.45	7429.00
0.3287	353.15	5823.00
0.3709	283.15	2223.00
0.3816	353.15	6569.00
0.3997	391.45	9439.00
0.4067	311.15	3968.00
0.4335	391.45	10014.00
0.4484	353.15	7815.00
0.4972	353.15	8435.00
0.5249	283.15	2940.00
0.5335	311.15	5014.00
0.5467	391.45	12133.00
0.5665	311.15	5225.00
0.6816	353.15	10649.00
0.6986	311.15	6064.00
0.6988	283.15	3532.00
0.7613	311.15	6429.00
0.7848	311.15	6644.00
0.7980	283.15	3783.00
0.8871	311.15	7191.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Toluene (1) - Gas	Vapor or sublimation pressure, kPa - Gas
343.20	0.1000	11270.00
353.20	0.1000	12290.00
363.20	0.1000	13110.00
373.20	0.1000	13740.00
383.20	0.1000	13980.00
393.20	0.1000	13980.00
403.20	0.1000	13570.00
403.20	0.2000	15860.00
413.20	0.2000	15990.00
420.50	0.1000	12430.00
423.20	0.2000	15990.00
424.50	0.1000	10600.00
425.30	0.1000	6770.00
426.80	0.1000	7670.00
427.40	0.1000	8620.00
433.20	0.2000	15710.00
433.20	0.3000	16580.00
443.20	0.2000	15070.00
443.20	0.3000	16490.00
451.00	0.2000	14340.00
453.20	0.3000	16340.00
463.20	0.3000	15820.00
466.80	0.2000	6790.00
468.70	0.2000	12420.00
472.20	0.2000	10650.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Toluene (1) - Gas	Vapor or sublimation pressure, kPa - Gas
473.20	0.2000	8620.00
473.20	0.3000	15100.00
473.20	0.4000	15690.00
483.00	0.3000	13880.00
483.00	0.4000	15170.00
493.00	0.4000	14400.00
493.00	0.5000	14570.00
494.00	0.3000	12460.00
496.00	0.3000	6770.00
497.00	0.3000	11540.00
499.00	0.3000	7690.00
499.00	0.5000	14090.00
501.00	0.3000	10600.00
502.00	0.3000	9670.00
502.00	0.3000	8620.00
504.00	0.4000	13370.00
510.00	0.4000	12440.00
516.00	0.4000	6790.00
520.00	0.5000	12470.00
521.00	0.4000	10600.00
522.00	0.4000	8650.00
534.00	0.5000	10620.00
535.00	0.5000	6770.00
539.00	0.5000	8620.00
548.00	0.6000	9640.00
550.00	0.6000	6770.00
552.00	0.6000	8620.00
553.00	0.7000	9020.00
557.00	0.7000	8600.00
563.00	0.7000	7690.00
564.00	0.7000	6770.00

Molar volume, m3/mol [ref]

Operational condition: Temperature, K = 323 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Molar volume, m3/mol - Liquid
0.0910	0.0001
0.1750	0.0001
0.2600	0.0001
0.3350	0.0001
0.4080	0.0001
0.4800	0.0001
0.5240	0.0001
0.5830	0.0001
0.6440	0.0001
0.7150	0.0001
0.7640	0.0001
0.8210	0.0001
0.8650	0.0001
0.8830	0.0001

Molar volume, m3/mol [ref]

Operational condition: Temperature, K = 323 (Liquid)

Mole fraction of Carbon dioxide (2) - Liquid	Molar volume, m3/mol - Liquid
0.0910	0.0001
0.1750	0.0001
0.2600	0.0001
0.3350	0.0001
0.4080	0.0001
0.4800	0.0001
0.5240	0.0001
0.5830	0.0001
0.6440	0.0001
0.7150	0.0001
0.7640	0.0001
0.8210	0.0001
0.8650	0.0001
0.8830	0.0001

Sources

• The experiments and correlations of the solubility of ethylene in toluene solvent
• A new high-pressure vapour liquid equilibrium apparatus
• Phase-equilibrium measurements with a novel multi-purpose high-pressure view cell: CO2 + n-decane and CO2 + toluene
• Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
• Pressure-Density-Temperature Behavior of CO2/Acetone, CO2/Toluene, and CO2/Monochlorobenzene Mixtures in the Near-Critical Region
• High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
• Phase Boundaries of CO2 + Toluene, CO2 + Acetone, and CO2 + Ethanol at High Temperatures and High Pressures
• Solubility of Ethylene in 2,2,4-Trimethylpentane at Various Temperatures and Pressures
• Measurement and Correlation of CO2 Solubility in the Systems of CO2 + Toluene, CO2 + Benzene, and CO2 + n-Hexane at Near-Critical and Supercritical Conditions
• Vapor-Liquid Equilibrium for Carbon Dioxide + Isopropyl, Isobutyl, and Isoamyl Acetates
• Measuring and Modeling the Solubility and Density for CO2 Toluene and C2H6 Toluene Systems
• Measurement and Correlation of Bubble Point Pressure in (CO2 + C6H6), (CO2 + CH3C6H5), (CO2 + C6H14), and (CO2 + C7H16) at Temperatures from (293.15 to 313.15) K