Mixture of Monoethanolamine + Carbon dioxide + Water

Datasets

1. Amount ratio of solute to solvent (32)
2. η - Viscosity, Pa*s (10)
3. σ_cond - Electrical conductivity, S/m (2)
4. P_vap - Vapor or sublimation pressure, kPa (4)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (16)
7. γ - Surface tension liquid-gas, N/m (4)

Amount ratio of solute to solvent of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313 (Liquid)
• Solvent: Mass fraction = 0.3 (Liquid)

Pressure, kPa - Liquid	Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid
116.00	0.0696
465.00	0.0797
659.00	0.0853
901.00	0.0886
1761.00	0.0965
3079.00	0.1021
5329.00	0.1111

Partial pressure, kPa of Carbon dioxide (2) [ref]

Operational condition: Molality, mol/kg = 7.02 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Partial pressure, kPa of Carbon dioxide (2) - Gas
313.15	2.202	0.07
313.15	2.929	0.29
313.15	3.655	6.40
313.15	3.949	22.40
313.15	4.229	61.80
313.15	4.483	113.80
313.15	4.77	203.20
313.15	5.029	316.00
333.15	0.7507	0.03
333.15	1.5337	0.17
333.15	2.2725	0.50
333.15	3.0043	3.11
333.15	3.687	41.40
333.15	3.9242	97.00
333.15	4.148	184.70
333.15	4.4034	340.40
373.15	1.1892	1.00
373.15	1.5822	3.50
373.15	1.9842	7.60
373.15	2.3617	14.60
373.15	2.7826	34.30
373.15	3.1924	86.80
373.15	3.5635	218.00
373.15	3.8645	436.10
393.15	0.7409	2.50
393.15	1.1219	8.60
393.15	1.4895	16.90
393.15	1.9337	34.50
393.15	2.3862	69.90
393.15	2.8261	148.30
393.15	3.2667	328.90

Mole fraction of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
0.30	0.9630	0.0100
1.18	0.9620	0.0110
13.26	0.9590	0.0140
45.16	0.9570	0.0160
106.71	0.9540	0.0190
173.23	0.9540	0.0200
257.40	0.9530	0.0210
353.44	0.9510	0.0220
428.30	0.9510	0.0220
569.65	0.9500	0.0230

Amount ratio of solute to solvent of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313.2 (Liquid)
• Mass ratio of solute to solvent = 5.536 (Liquid)

Pressure, kPa - Liquid	Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid
14.20	0.5540
34.40	0.6230
88.40	0.6720
150.10	0.7350
243.10	0.7850
353.40	0.8240
441.40	0.8450
539.70	0.8560
655.20	0.8650
746.50	0.8710
829.80	0.8760
915.30	0.8870

Mass fraction of Carbon dioxide (2) [ref]

Operational conditions:

• Solvent: Mass fraction = 0.153 (Liquid)
• Temperature, K = 313.2 (Liquid)

Pressure, kPa of Carbon dioxide (2) - Gas	Mass fraction of Carbon dioxide (2) - Liquid
7.00	0.0525
7.20	0.0533
14.60	0.0578
19.10	0.0582
32.00	0.0628
59.90	0.0670
93.80	0.0695
152.80	0.0752
240.70	0.0772
362.30	0.0809
462.70	0.0835
562.20	0.0845
762.40	0.0865
846.90	0.0887
994.40	0.0897

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313.2 (Liquid)
• Molality, mol/kg = 7.016 (Liquid)

Pressure, kPa of Carbon dioxide (2) - Gas	Molality, mol/kg of Carbon dioxide (2) - Liquid
14.02	3.688
11.71	3.628
5.41	3.49
4.23	3.469
3.62	3.431
2.59	3.413
2.01	3.358
0.38	3.024
0.26	2.853

Mass ratio of solute to solvent of Carbon dioxide (2) [ref]

Fixed			Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Temperature, K - Liquid	Pressure, kPa - Liquid	Mass ratio of solute to solvent of Carbon dioxide (2) - Liquid
0.2200	313.20	100.00	0.0962

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313.2 (Liquid)
• Solvent: Mass fraction = 0.153 (Liquid)

Pressure, kPa - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid
8.31	1.3
9.69	1.413
12.98	1.513
16.57	1.573
20.52	1.619
24.04	1.652
28.65	1.687
35.04	1.729
41.29	1.763
49.41	1.802
58.47	1.838
67.51	1.87

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational condition: Solvent: Mass fraction = 0.302 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid
313.00	10.60	2.329
313.00	18.11	2.5
313.00	40.61	2.657
313.00	69.80	2.781
313.00	105.70	2.89
313.00	160.70	3.016
373.00	97.52	1.304
373.00	105.95	1.62
373.00	151.90	2.047
373.00	215.20	2.241
373.00	279.30	2.35

Mass fraction of Carbon dioxide (2) [ref]

Operational condition: Solvent: Mass fraction = 0.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa of Carbon dioxide (2) - Gas	Mass fraction of Carbon dioxide (2) - Liquid
313.30	8.60	0.1020
313.30	6.80	0.1010
313.20	2.80	0.0970
313.20	0.86	0.0900
313.20	0.57	0.0890
313.20	0.26	0.0840
313.30	21.30	0.1070
313.40	5.90	0.1020
313.30	2.20	0.0970
313.30	0.65	0.0910
313.30	0.33	0.0880
313.30	13.60	0.1060
313.40	2.60	0.1000
313.40	1.30	0.0960
313.40	0.50	0.0900
313.40	0.27	0.0850
313.20	10.50	0.0996
313.20	31.20	0.1074
313.20	77.30	0.1147
313.20	154.70	0.1216
313.10	265.90	0.1278
313.10	19.20	0.1066
313.20	56.40	0.1140
313.20	122.00	0.1209
313.10	219.60	0.1272
313.20	351.20	0.1329
313.20	516.30	0.1381
393.10	8.50	0.0382
393.10	13.60	0.0455
393.10	21.20	0.0526
393.10	32.70	0.0596
393.10	50.30	0.0664
393.10	77.50	0.0731
393.10	121.40	0.0793
393.10	190.10	0.0851
393.10	296.00	0.0904
393.10	5.30	0.0308
393.10	10.20	0.0405
393.10	18.10	0.0498
393.10	32.40	0.0585
393.20	49.90	0.0653
393.10	72.80	0.0710
393.20	93.30	0.0745
393.20	132.60	0.0792
393.10	189.80	0.0837
393.20	225.40	0.0859
393.20	271.20	0.0881
393.10	308.20	0.0896
393.10	334.20	0.0905
393.20	351.30	0.0911

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 313.2 (Liquid)

Fixed		Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Pressure, kPa of Carbon dioxide (2) - Gas	Molality, mol/kg of Carbon dioxide (2) - Liquid
0.1530	1.29	1.102
0.1530	2.67	1.197
0.1530	5.97	1.283
0.1530	13.51	1.373
0.1530	34.27	1.493
0.1530	60.49	1.586
0.1500	1.92	1.098
0.1500	3.24	1.208
0.1500	7.45	1.309
0.1500	14.11	1.392
0.1500	21.88	1.444
0.1500	35.71	1.513
0.1500	53.70	1.579
0.1500	73.95	1.633
0.1500	91.43	1.675

Mole fraction of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313.15 (Liquid)
• Solvent: Mass fraction = 0.153 (Liquid)

Pressure, kPa of Carbon dioxide (2) - Gas	Mole fraction of Carbon dioxide (2) - Liquid
1.30	0.0222
3.00	0.0239
6.50	0.0255
25.10	0.0281
46.70	0.0305
134.50	0.0337
343.30	0.0372
701.60	0.0417
1554.50	0.0458

Mass ratio of solute to solvent of Carbon dioxide (2) [ref]

Fixed			Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Temperature, K - Liquid	Pressure, kPa - Liquid	Mass ratio of solute to solvent of Carbon dioxide (2) - Liquid
0.3002	303.15	1500.00	0.1590

Mole fraction of Carbon dioxide (2) [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
313.15	0.10	0.0497	0.0173
313.15	0.30	0.0496	0.0195
313.15	0.80	0.0495	0.0217
313.15	2.40	0.0494	0.0237
313.15	16.00	0.0492	0.0271
313.15	65.00	0.0490	0.0311
313.15	182.00	0.0488	0.0351
313.15	402.70	0.0486	0.0391
373.15	0.50	0.0503	0.0047
373.15	2.10	0.0502	0.0082
373.15	4.10	0.0500	0.0112
373.15	9.90	0.0498	0.0148
373.15	20.70	0.0497	0.0178
373.15	47.30	0.0495	0.0211
373.15	129.40	0.0493	0.0253
373.15	290.00	0.0491	0.0288

Molality, mol/kg of Carbon dioxide (2) [ref]

Fixed			Measured
Temperature, K - Liquid	Molality, mol/kg of Monoethanolamine (1) - Liquid	Pressure, kPa of Carbon dioxide (2) - Gas	Molality, mol/kg of Carbon dioxide (2) - Liquid
313.63	2.856	1813.00	2.863
313.27	2.911	2134.00	2.962
313.22	2.911	2770.00	3.125
313.21	2.911	3450.00	3.216
313.11	2.889	5240.00	3.541
313.20	2.931	8070.00	3.76
353.14	2.93	803.00	2.111
353.23	2.93	970.00	2.156
353.15	2.93	1198.00	2.244
353.18	2.93	1623.00	2.374
353.19	2.93	2400.00	2.548
353.20	2.93	3100.00	2.665
353.24	2.93	3470.00	2.732
353.20	2.93	4340.00	2.836
353.17	2.93	4750.00	2.899
353.23	2.93	6350.00	3.08
393.11	2.856	786.00	1.518
393.16	2.856	1359.00	1.72
393.15	2.856	2111.00	1.894
393.14	2.856	2490.00	1.992
393.15	2.856	3300.00	2.087
393.17	2.856	3650.00	2.17
393.15	2.856	4670.00	2.308
393.15	2.856	5440.00	2.425
393.16	2.856	6580.00	2.52
393.16	2.856	8740.00	2.699
313.23	7.008	448.00	4.98
313.24	7.008	695.00	5.267
313.24	7.008	739.00	5.261
313.18	7.069	745.00	5.405
313.23	7.008	1312.00	5.739
313.26	7.008	1671.00	5.965
313.24	7.008	3620.00	6.627
313.23	7.008	4920.00	6.855
313.25	7.008	7320.00	7.233
313.20	7.008	7510.00	7.279
353.26	7.069	513.00	4.151
353.16	7.069	981.00	4.544
353.17	7.069	1715.00	4.862
353.18	7.069	2234.00	5.027
353.16	7.069	2710.00	5.182
353.15	7.069	3800.00	5.457
353.21	7.069	5520.00	5.732
353.18	7.069	7400.00	6.059
393.14	7.069	644.00	3.37
393.19	7.069	972.00	3.603
393.19	7.069	1249.00	3.731
393.19	7.069	2084.00	3.995
393.21	7.069	2760.00	4.148
393.18	7.069	3230.00	4.255
393.19	7.069	3410.00	4.316
393.21	7.069	4210.00	4.483
393.19	7.069	5230.00	4.709
393.16	7.069	7230.00	4.987
313.16	2.863	2.30	1.417
313.16	2.863	5.94	1.521
313.18	2.869	9.93	1.585
313.16	2.863	14.70	1.638
313.17	2.869	21.70	1.689
313.16	2.863	28.10	1.732
313.17	2.869	39.90	1.788
313.18	2.869	56.20	1.84
353.16	2.872	1.59	0.7500
353.17	2.893	2.79	0.8720
353.17	2.893	5.17	1.029
353.17	2.872	8.01	1.12
353.17	2.893	12.80	1.226
353.17	2.872	20.40	1.322
353.17	2.893	23.90	1.364
353.17	2.872	49.40	1.492
353.16	2.893	59.90	1.531
393.20	2.818	2.06	0.2050
393.16	2.818	3.49	0.3150
393.17	2.999	5.65	0.4390
393.14	2.999	11.30	0.6120
393.18	2.999	19.90	0.7530
393.11	2.999	26.00	0.8290
393.19	2.818	49.10	0.9320
393.17	2.999	38.90	0.9340
393.18	2.818	74.00	1.02
393.17	2.999	58.20	1.038
313.20	7.055	1.38	3.296
313.16	7.097	3.27	3.498
313.21	6.919	6.08	3.519
313.21	7.055	9.02	3.679
313.21	7.097	17.50	3.826
313.21	7.097	29.20	3.958
313.16	7.035	49.10	4.061
313.21	6.919	66.40	4.106
352.86	7.192	1.58	2.105
352.83	6.992	3.75	2.462
352.81	7.036	6.59	2.787
352.83	6.992	11.80	3.002
352.85	7.192	18.40	3.204
352.81	7.036	23.00	3.228
352.84	6.992	29.60	3.289
352.82	6.992	39.70	3.4
352.83	6.992	55.20	3.489
352.83	7.019	70.40	3.591
352.83	7.019	78.70	3.622
391.99	7.109	2.92	0.7300
391.99	7.338	3.10	0.8450
391.98	7.338	4.24	0.9690
392.03	7.251	7.16	1.239
392.00	7.338	12.20	1.564
391.94	7.109	16.00	1.704
392.00	7.338	24.20	2.004
391.98	7.338	27.60	2.087
392.00	7.338	41.60	2.369
392.01	7.109	62.40	2.497
392.01	7.251	69.80	2.618
391.96	7.251	73.20	2.633

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational condition: Molality, mol/kg = 7.017 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid
313.15	9.60	3.485
313.15	36.00	4.086
313.15	142.80	4.65
313.15	336.70	5.115
313.15	586.60	5.474
353.15	48.40	2.476
353.15	56.30	3.054
353.15	82.00	3.478
353.15	176.60	3.901
353.15	303.10	4.159
353.15	477.00	4.387
353.15	551.50	4.472
353.15	579.50	4.506
393.15	178.10	0.4800
393.15	181.40	0.9670
393.15	187.60	1.452
393.15	199.20	1.909
393.15	212.30	2.209
393.15	234.70	2.502
393.15	270.70	2.79
393.15	332.80	3.063
393.15	434.60	3.348
393.15	587.20	3.595

Amount ratio of solute to solvent of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313 (Liquid)
• Solvent: Mass fraction = 0.3 (Liquid)

Pressure, kPa - Liquid	Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid
116.00	0.0696
465.00	0.0797
659.00	0.0853
901.00	0.0886
1761.00	0.0965
3079.00	0.1021
5329.00	0.1111

Partial pressure, kPa of Carbon dioxide (2) [ref]

Operational condition: Molality, mol/kg = 7.02 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Partial pressure, kPa of Carbon dioxide (2) - Gas
313.15	2.202	0.07
313.15	2.929	0.29
313.15	3.655	6.40
313.15	3.949	22.40
313.15	4.229	61.80
313.15	4.483	113.80
313.15	4.77	203.20
313.15	5.029	316.00
333.15	0.7507	0.03
333.15	1.5337	0.17
333.15	2.2725	0.50
333.15	3.0043	3.11
333.15	3.687	41.40
333.15	3.9242	97.00
333.15	4.148	184.70
333.15	4.4034	340.40
373.15	1.1892	1.00
373.15	1.5822	3.50
373.15	1.9842	7.60
373.15	2.3617	14.60
373.15	2.7826	34.30
373.15	3.1924	86.80
373.15	3.5635	218.00
373.15	3.8645	436.10
393.15	0.7409	2.50
393.15	1.1219	8.60
393.15	1.4895	16.90
393.15	1.9337	34.50
393.15	2.3862	69.90
393.15	2.8261	148.30
393.15	3.2667	328.90

Mole fraction of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
0.30	0.9630	0.0100
1.18	0.9620	0.0110
13.26	0.9590	0.0140
45.16	0.9570	0.0160
106.71	0.9540	0.0190
173.23	0.9540	0.0200
257.40	0.9530	0.0210
353.44	0.9510	0.0220
428.30	0.9510	0.0220
569.65	0.9500	0.0230

Amount ratio of solute to solvent of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313.2 (Liquid)
• Mass ratio of solute to solvent = 5.536 (Liquid)

Pressure, kPa - Liquid	Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid
14.20	0.5540
34.40	0.6230
88.40	0.6720
150.10	0.7350
243.10	0.7850
353.40	0.8240
441.40	0.8450
539.70	0.8560
655.20	0.8650
746.50	0.8710
829.80	0.8760
915.30	0.8870

Mass fraction of Carbon dioxide (2) [ref]

Operational conditions:

• Solvent: Mass fraction = 0.153 (Liquid)
• Temperature, K = 313.2 (Liquid)

Pressure, kPa of Carbon dioxide (2) - Gas	Mass fraction of Carbon dioxide (2) - Liquid
7.00	0.0525
7.20	0.0533
14.60	0.0578
19.10	0.0582
32.00	0.0628
59.90	0.0670
93.80	0.0695
152.80	0.0752
240.70	0.0772
362.30	0.0809
462.70	0.0835
562.20	0.0845
762.40	0.0865
846.90	0.0887
994.40	0.0897

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313.2 (Liquid)
• Molality, mol/kg = 7.016 (Liquid)

Pressure, kPa of Carbon dioxide (2) - Gas	Molality, mol/kg of Carbon dioxide (2) - Liquid
14.02	3.688
11.71	3.628
5.41	3.49
4.23	3.469
3.62	3.431
2.59	3.413
2.01	3.358
0.38	3.024
0.26	2.853

Mass ratio of solute to solvent of Carbon dioxide (2) [ref]

Fixed			Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Temperature, K - Liquid	Pressure, kPa - Liquid	Mass ratio of solute to solvent of Carbon dioxide (2) - Liquid
0.2200	313.20	100.00	0.0962

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313.2 (Liquid)
• Solvent: Mass fraction = 0.153 (Liquid)

Pressure, kPa - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid
8.31	1.3
9.69	1.413
12.98	1.513
16.57	1.573
20.52	1.619
24.04	1.652
28.65	1.687
35.04	1.729
41.29	1.763
49.41	1.802
58.47	1.838
67.51	1.87

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational condition: Solvent: Mass fraction = 0.302 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid
313.00	10.60	2.329
313.00	18.11	2.5
313.00	40.61	2.657
313.00	69.80	2.781
313.00	105.70	2.89
313.00	160.70	3.016
373.00	97.52	1.304
373.00	105.95	1.62
373.00	151.90	2.047
373.00	215.20	2.241
373.00	279.30	2.35

Mass fraction of Carbon dioxide (2) [ref]

Operational condition: Solvent: Mass fraction = 0.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa of Carbon dioxide (2) - Gas	Mass fraction of Carbon dioxide (2) - Liquid
313.30	8.60	0.1020
313.30	6.80	0.1010
313.20	2.80	0.0970
313.20	0.86	0.0900
313.20	0.57	0.0890
313.20	0.26	0.0840
313.30	21.30	0.1070
313.40	5.90	0.1020
313.30	2.20	0.0970
313.30	0.65	0.0910
313.30	0.33	0.0880
313.30	13.60	0.1060
313.40	2.60	0.1000
313.40	1.30	0.0960
313.40	0.50	0.0900
313.40	0.27	0.0850
313.20	10.50	0.0996
313.20	31.20	0.1074
313.20	77.30	0.1147
313.20	154.70	0.1216
313.10	265.90	0.1278
313.10	19.20	0.1066
313.20	56.40	0.1140
313.20	122.00	0.1209
313.10	219.60	0.1272
313.20	351.20	0.1329
313.20	516.30	0.1381
393.10	8.50	0.0382
393.10	13.60	0.0455
393.10	21.20	0.0526
393.10	32.70	0.0596
393.10	50.30	0.0664
393.10	77.50	0.0731
393.10	121.40	0.0793
393.10	190.10	0.0851
393.10	296.00	0.0904
393.10	5.30	0.0308
393.10	10.20	0.0405
393.10	18.10	0.0498
393.10	32.40	0.0585
393.20	49.90	0.0653
393.10	72.80	0.0710
393.20	93.30	0.0745
393.20	132.60	0.0792
393.10	189.80	0.0837
393.20	225.40	0.0859
393.20	271.20	0.0881
393.10	308.20	0.0896
393.10	334.20	0.0905
393.20	351.30	0.0911

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational condition: Temperature, K = 313.2 (Liquid)

Fixed		Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Pressure, kPa of Carbon dioxide (2) - Gas	Molality, mol/kg of Carbon dioxide (2) - Liquid
0.1530	1.29	1.102
0.1530	2.67	1.197
0.1530	5.97	1.283
0.1530	13.51	1.373
0.1530	34.27	1.493
0.1530	60.49	1.586
0.1500	1.92	1.098
0.1500	3.24	1.208
0.1500	7.45	1.309
0.1500	14.11	1.392
0.1500	21.88	1.444
0.1500	35.71	1.513
0.1500	53.70	1.579
0.1500	73.95	1.633
0.1500	91.43	1.675

Mole fraction of Carbon dioxide (2) [ref]

Operational conditions:

• Temperature, K = 313.15 (Liquid)
• Solvent: Mass fraction = 0.153 (Liquid)

Pressure, kPa of Carbon dioxide (2) - Gas	Mole fraction of Carbon dioxide (2) - Liquid
1.30	0.0222
3.00	0.0239
6.50	0.0255
25.10	0.0281
46.70	0.0305
134.50	0.0337
343.30	0.0372
701.60	0.0417
1554.50	0.0458

Mass ratio of solute to solvent of Carbon dioxide (2) [ref]

Fixed			Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Temperature, K - Liquid	Pressure, kPa - Liquid	Mass ratio of solute to solvent of Carbon dioxide (2) - Liquid
0.3002	303.15	1500.00	0.1590

Mole fraction of Carbon dioxide (2) [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid
313.15	0.10	0.0497	0.0173
313.15	0.30	0.0496	0.0195
313.15	0.80	0.0495	0.0217
313.15	2.40	0.0494	0.0237
313.15	16.00	0.0492	0.0271
313.15	65.00	0.0490	0.0311
313.15	182.00	0.0488	0.0351
313.15	402.70	0.0486	0.0391
373.15	0.50	0.0503	0.0047
373.15	2.10	0.0502	0.0082
373.15	4.10	0.0500	0.0112
373.15	9.90	0.0498	0.0148
373.15	20.70	0.0497	0.0178
373.15	47.30	0.0495	0.0211
373.15	129.40	0.0493	0.0253
373.15	290.00	0.0491	0.0288

Molality, mol/kg of Carbon dioxide (2) [ref]

Fixed			Measured
Temperature, K - Liquid	Molality, mol/kg of Monoethanolamine (1) - Liquid	Pressure, kPa of Carbon dioxide (2) - Gas	Molality, mol/kg of Carbon dioxide (2) - Liquid
313.63	2.856	1813.00	2.863
313.27	2.911	2134.00	2.962
313.22	2.911	2770.00	3.125
313.21	2.911	3450.00	3.216
313.11	2.889	5240.00	3.541
313.20	2.931	8070.00	3.76
353.14	2.93	803.00	2.111
353.23	2.93	970.00	2.156
353.15	2.93	1198.00	2.244
353.18	2.93	1623.00	2.374
353.19	2.93	2400.00	2.548
353.20	2.93	3100.00	2.665
353.24	2.93	3470.00	2.732
353.20	2.93	4340.00	2.836
353.17	2.93	4750.00	2.899
353.23	2.93	6350.00	3.08
393.11	2.856	786.00	1.518
393.16	2.856	1359.00	1.72
393.15	2.856	2111.00	1.894
393.14	2.856	2490.00	1.992
393.15	2.856	3300.00	2.087
393.17	2.856	3650.00	2.17
393.15	2.856	4670.00	2.308
393.15	2.856	5440.00	2.425
393.16	2.856	6580.00	2.52
393.16	2.856	8740.00	2.699
313.23	7.008	448.00	4.98
313.24	7.008	695.00	5.267
313.24	7.008	739.00	5.261
313.18	7.069	745.00	5.405
313.23	7.008	1312.00	5.739
313.26	7.008	1671.00	5.965
313.24	7.008	3620.00	6.627
313.23	7.008	4920.00	6.855
313.25	7.008	7320.00	7.233
313.20	7.008	7510.00	7.279
353.26	7.069	513.00	4.151
353.16	7.069	981.00	4.544
353.17	7.069	1715.00	4.862
353.18	7.069	2234.00	5.027
353.16	7.069	2710.00	5.182
353.15	7.069	3800.00	5.457
353.21	7.069	5520.00	5.732
353.18	7.069	7400.00	6.059
393.14	7.069	644.00	3.37
393.19	7.069	972.00	3.603
393.19	7.069	1249.00	3.731
393.19	7.069	2084.00	3.995
393.21	7.069	2760.00	4.148
393.18	7.069	3230.00	4.255
393.19	7.069	3410.00	4.316
393.21	7.069	4210.00	4.483
393.19	7.069	5230.00	4.709
393.16	7.069	7230.00	4.987
313.16	2.863	2.30	1.417
313.16	2.863	5.94	1.521
313.18	2.869	9.93	1.585
313.16	2.863	14.70	1.638
313.17	2.869	21.70	1.689
313.16	2.863	28.10	1.732
313.17	2.869	39.90	1.788
313.18	2.869	56.20	1.84
353.16	2.872	1.59	0.7500
353.17	2.893	2.79	0.8720
353.17	2.893	5.17	1.029
353.17	2.872	8.01	1.12
353.17	2.893	12.80	1.226
353.17	2.872	20.40	1.322
353.17	2.893	23.90	1.364
353.17	2.872	49.40	1.492
353.16	2.893	59.90	1.531
393.20	2.818	2.06	0.2050
393.16	2.818	3.49	0.3150
393.17	2.999	5.65	0.4390
393.14	2.999	11.30	0.6120
393.18	2.999	19.90	0.7530
393.11	2.999	26.00	0.8290
393.19	2.818	49.10	0.9320
393.17	2.999	38.90	0.9340
393.18	2.818	74.00	1.02
393.17	2.999	58.20	1.038
313.20	7.055	1.38	3.296
313.16	7.097	3.27	3.498
313.21	6.919	6.08	3.519
313.21	7.055	9.02	3.679
313.21	7.097	17.50	3.826
313.21	7.097	29.20	3.958
313.16	7.035	49.10	4.061
313.21	6.919	66.40	4.106
352.86	7.192	1.58	2.105
352.83	6.992	3.75	2.462
352.81	7.036	6.59	2.787
352.83	6.992	11.80	3.002
352.85	7.192	18.40	3.204
352.81	7.036	23.00	3.228
352.84	6.992	29.60	3.289
352.82	6.992	39.70	3.4
352.83	6.992	55.20	3.489
352.83	7.019	70.40	3.591
352.83	7.019	78.70	3.622
391.99	7.109	2.92	0.7300
391.99	7.338	3.10	0.8450
391.98	7.338	4.24	0.9690
392.03	7.251	7.16	1.239
392.00	7.338	12.20	1.564
391.94	7.109	16.00	1.704
392.00	7.338	24.20	2.004
391.98	7.338	27.60	2.087
392.00	7.338	41.60	2.369
392.01	7.109	62.40	2.497
392.01	7.251	69.80	2.618
391.96	7.251	73.20	2.633

Molality, mol/kg of Carbon dioxide (2) [ref]

Operational condition: Molality, mol/kg = 7.017 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid
313.15	9.60	3.485
313.15	36.00	4.086
313.15	142.80	4.65
313.15	336.70	5.115
313.15	586.60	5.474
353.15	48.40	2.476
353.15	56.30	3.054
353.15	82.00	3.478
353.15	176.60	3.901
353.15	303.10	4.159
353.15	477.00	4.387
353.15	551.50	4.472
353.15	579.50	4.506
393.15	178.10	0.4800
393.15	181.40	0.9670
393.15	187.60	1.452
393.15	199.20	1.909
393.15	212.30	2.209
393.15	234.70	2.502
393.15	270.70	2.79
393.15	332.80	3.063
393.15	434.60	3.348
393.15	587.20	3.595

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Viscosity, Pa*s - Liquid
0.2000	0.0070	0.0017
0.2000	0.0140	0.0019
0.2000	0.0200	0.0019
0.2000	0.0270	0.0021
0.2000	0.0330	0.0023
0.3000	0.0110	0.0025
0.3000	0.0220	0.0028
0.3000	0.0330	0.0032
0.3000	0.0430	0.0034
0.3000	0.0530	0.0040
0.4000	0.0160	0.0039
0.4000	0.0320	0.0047
0.4000	0.0470	0.0052
0.4000	0.0620	0.0059
0.4000	0.0760	0.0069

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Solvent: Mass fraction = 0.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0025
298.15	0.6900	0.0028
298.15	1.23	0.0030
298.15	1.87	0.0033
298.15	2.41	0.0037
303.15	0.0000	0.0022
303.15	0.6900	0.0024
303.15	1.23	0.0025
303.15	1.87	0.0028
303.15	2.41	0.0032
313.15	0.0000	0.0017
313.15	0.6900	0.0019
313.15	1.23	0.0019
313.15	1.87	0.0022
313.15	2.41	0.0025
323.15	0.0000	0.0013
323.15	0.6900	0.0015
323.15	1.23	0.0016
323.15	1.87	0.0017
323.15	2.41	0.0020
333.15	0.0000	0.0011
333.15	0.6900	0.0012
333.15	1.23	0.0013
333.15	1.87	0.0014
343.15	0.0000	0.0009
343.15	0.6900	0.0010
343.15	1.23	0.0011
353.15	0.0000	0.0008
353.15	0.6900	0.0009
353.15	1.23	0.0009

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Fixed		Measured
Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid	Mass ratio of solute to solvent of Water (3) - Liquid	Viscosity, Pa*s - Liquid
0.0000	4.0	0.0017
0.1500	4.0	0.0018
0.2500	4.0	0.0019
0.3500	4.0	0.0021
0.5000	4.0	0.0022
0.0000	2.333	0.0026
0.1500	2.333	0.0029
0.2500	2.333	0.0031
0.3500	2.333	0.0033
0.5000	2.333	0.0039
0.0000	1.5	0.0035
0.1500	1.5	0.0042
0.2500	1.5	0.0047
0.3500	1.5	0.0057
0.5000	1.5	0.0067

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0620	0.0000	293.15	0.0012
0.0620	0.0000	293.15	0.0012
0.0620	0.0000	303.15	0.0010
0.0620	0.0000	303.15	0.0010
0.0620	0.0000	313.15	0.0008
0.0620	0.0000	313.15	0.0008
0.0620	0.0000	323.15	0.0007
0.0620	0.0000	323.15	0.0007
0.0620	0.0000	333.15	0.0006
0.0620	0.0000	333.15	0.0006
0.0620	0.0068	293.15	0.0012
0.0620	0.0068	293.15	0.0012
0.0620	0.0068	303.15	0.0010
0.0620	0.0068	303.15	0.0010
0.0620	0.0068	313.15	0.0008
0.0620	0.0068	313.15	0.0008
0.0620	0.0068	323.15	0.0007
0.0620	0.0068	323.15	0.0007
0.0620	0.0068	333.15	0.0006
0.0620	0.0068	333.15	0.0006
0.0620	0.0091	293.15	0.0013
0.0620	0.0091	293.15	0.0013
0.0620	0.0091	303.15	0.0010
0.0620	0.0091	303.15	0.0010
0.0620	0.0091	313.15	0.0008
0.0620	0.0091	313.15	0.0008
0.0620	0.0091	323.15	0.0007
0.0620	0.0091	323.15	0.0007
0.0620	0.0091	333.15	0.0006
0.0620	0.0091	333.15	0.0006
0.3000	0.0000	293.15	0.0029
0.3000	0.0000	293.15	0.0029
0.3000	0.0000	298.15	0.0024
0.3000	0.0000	298.15	0.0025
0.3000	0.0000	303.15	0.0021
0.3000	0.0000	303.15	0.0021
0.3000	0.0000	313.15	0.0016
0.3000	0.0000	313.15	0.0016
0.3000	0.0000	323.15	0.0013
0.3000	0.0000	323.15	0.0013
0.3000	0.0000	333.15	0.0011
0.3000	0.0000	333.15	0.0011
0.3000	0.0000	343.15	0.0009
0.3000	0.0000	343.15	0.0009
0.3000	0.0000	353.15	0.0007
0.3000	0.0000	353.15	0.0007
0.3000	0.0130	293.15	0.0031
0.3000	0.0130	293.15	0.0031
0.3000	0.0130	298.15	0.0027
0.3000	0.0130	298.15	0.0026
0.3000	0.0130	303.15	0.0023
0.3000	0.0130	303.15	0.0023
0.3000	0.0130	313.15	0.0018
0.3000	0.0130	313.15	0.0018
0.3000	0.0130	323.15	0.0014
0.3000	0.0130	323.15	0.0014
0.3000	0.0130	333.15	0.0011
0.3000	0.0130	333.15	0.0011
0.3000	0.0130	343.15	0.0010
0.3000	0.0130	343.15	0.0010
0.3000	0.0130	353.15	0.0008
0.3000	0.0130	353.15	0.0008
0.3000	0.0215	293.15	0.0033
0.3000	0.0215	293.15	0.0033
0.3000	0.0215	298.15	0.0028
0.3000	0.0215	298.15	0.0028
0.3000	0.0215	303.15	0.0024
0.3000	0.0215	303.15	0.0024
0.3000	0.0215	313.15	0.0019
0.3000	0.0215	313.15	0.0019
0.3000	0.0215	323.15	0.0015
0.3000	0.0215	323.15	0.0015
0.3000	0.0215	333.15	0.0012
0.3000	0.0215	333.15	0.0012
0.3000	0.0215	343.15	0.0010
0.3000	0.0215	343.15	0.0010
0.3000	0.0215	353.15	0.0009
0.3000	0.0215	353.15	0.0009
0.3000	0.0328	293.15	0.0036
0.3000	0.0328	293.15	0.0036
0.3000	0.0328	298.15	0.0031
0.3000	0.0328	298.15	0.0031
0.3000	0.0328	303.15	0.0027
0.3000	0.0328	303.15	0.0027
0.3000	0.0328	313.15	0.0021
0.3000	0.0328	313.15	0.0021
0.3000	0.0328	323.15	0.0017
0.3000	0.0328	323.15	0.0017
0.3000	0.0328	333.15	0.0014
0.3000	0.0328	333.15	0.0014
0.3000	0.0328	343.15	0.0011
0.3000	0.0328	343.15	0.0012
0.3000	0.0328	353.15	0.0010
0.3000	0.0328	353.15	0.0010
0.3000	0.0431	293.15	0.0039
0.3000	0.0431	293.15	0.0039
0.3000	0.0431	298.15	0.0033
0.3000	0.0431	298.15	0.0033
0.3000	0.0431	303.15	0.0029
0.3000	0.0431	303.15	0.0029
0.3000	0.0431	313.15	0.0022
0.3000	0.0431	313.15	0.0022
0.3000	0.0431	323.15	0.0018
0.3000	0.0431	323.15	0.0018
0.3000	0.0431	333.15	0.0015
0.3000	0.0431	333.15	0.0015
0.3000	0.0431	343.15	0.0013
0.3000	0.0431	343.15	0.0013
0.3000	0.0431	353.15	0.0011
0.3000	0.0431	353.15	0.0011
0.3000	0.0544	293.15	0.0043
0.3000	0.0544	293.15	0.0043
0.3000	0.0544	298.15	0.0037
0.3000	0.0544	298.15	0.0037
0.3000	0.0544	303.15	0.0032
0.3000	0.0544	303.15	0.0032
0.3000	0.0544	313.15	0.0025
0.3000	0.0544	313.15	0.0025
0.3000	0.0544	323.15	0.0020
0.3000	0.0544	323.15	0.0020
0.3000	0.0544	333.15	0.0016
0.3000	0.0544	333.15	0.0016
0.3000	0.0544	343.15	0.0013
0.3000	0.0544	343.15	0.0014
0.3000	0.0544	353.15	0.0011
0.3000	0.0544	353.15	0.0011

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0687	0.0017
298.15	0.0000	0.1122	0.0025
298.15	0.0000	0.1643	0.0036
298.15	0.0000	0.2278	0.0055
298.15	0.0000	0.4076	0.0125
298.15	0.0000	0.7264	0.0194
298.15	0.0000	1.0000	0.0199
298.15	0.0068	0.0682	0.0018
298.15	0.0111	0.1152	0.0026
298.15	0.0135	0.0677	0.0019
298.15	0.0162	0.1759	0.0040
298.15	0.0202	0.0673	0.0019
298.15	0.0220	0.1139	0.0029
298.15	0.0267	0.0668	0.0021
298.15	0.0318	0.1728	0.0046
298.15	0.0326	0.1126	0.0031
298.15	0.0332	0.0664	0.0022
298.15	0.0430	0.1114	0.0035
298.15	0.0470	0.1699	0.0051
298.15	0.0531	0.1101	0.0039
298.15	0.0617	0.1671	0.0060
298.15	0.0759	0.1643	0.0070
313.15	0.0000	0.0687	0.0012
313.15	0.0000	0.1122	0.0017
313.15	0.0000	0.1643	0.0023
313.15	0.0000	0.2278	0.0034
313.15	0.0000	0.4076	0.0070
313.15	0.0000	0.7264	0.0102
313.15	0.0000	1.0000	0.0096
313.15	0.0068	0.0682	0.0013
313.15	0.0111	0.1152	0.0017
313.15	0.0135	0.0677	0.0013
313.15	0.0162	0.1759	0.0025
313.15	0.0202	0.0673	0.0013
313.15	0.0220	0.1139	0.0020
313.15	0.0267	0.0668	0.0014
313.15	0.0318	0.1728	0.0030
313.15	0.0326	0.1126	0.0020
313.15	0.0332	0.0664	0.0016
313.15	0.0430	0.1114	0.0024
313.15	0.0470	0.1699	0.0033
313.15	0.0531	0.1101	0.0027
313.15	0.0617	0.1671	0.0040
313.15	0.0759	0.1643	0.0046
323.15	0.0000	0.0687	0.0009
323.15	0.0000	0.1122	0.0013
323.15	0.0000	0.1643	0.0018
323.15	0.0000	0.2278	0.0025
323.15	0.0000	0.4076	0.0049
323.15	0.0000	0.7264	0.0071
323.15	0.0000	1.0000	0.0067
323.15	0.0068	0.0682	0.0010
323.15	0.0111	0.1152	0.0014
323.15	0.0135	0.0677	0.0010
323.15	0.0162	0.1759	0.0020
323.15	0.0202	0.0673	0.0011
323.15	0.0220	0.1139	0.0016
323.15	0.0267	0.0668	0.0012
323.15	0.0318	0.1728	0.0023
323.15	0.0326	0.1126	0.0016
323.15	0.0332	0.0664	0.0013
323.15	0.0430	0.1114	0.0019
323.15	0.0470	0.1699	0.0026
323.15	0.0531	0.1101	0.0021
323.15	0.0617	0.1671	0.0031
323.15	0.0759	0.1643	0.0038
343.15	0.0000	0.0687	0.0007
343.15	0.0000	0.1122	0.0009
343.15	0.0000	0.1643	0.0011
343.15	0.0000	0.2278	0.0016
343.15	0.0000	0.4076	0.0028
343.15	0.0000	0.7264	0.0038
343.15	0.0000	1.0000	0.0037
343.15	0.0068	0.0682	0.0007
343.15	0.0111	0.1152	0.0009
343.15	0.0135	0.0677	0.0007
343.15	0.0162	0.1759	0.0013
343.15	0.0202	0.0673	0.0008
343.15	0.0220	0.1139	0.0011
343.15	0.0267	0.0668	0.0008
343.15	0.0318	0.1728	0.0015
343.15	0.0326	0.1126	0.0011
343.15	0.0332	0.0664	0.0009
343.15	0.0430	0.1114	0.0013
343.15	0.0470	0.1699	0.0017
343.15	0.0531	0.1101	0.0015
343.15	0.0617	0.1671	0.0020
343.15	0.0759	0.1643	0.0023
353.15	0.0000	0.0687	0.0006
353.15	0.0000	0.1122	0.0008
353.15	0.0000	0.1643	0.0009
353.15	0.0000	0.2278	0.0013
353.15	0.0000	0.4076	0.0022
353.15	0.0000	0.7264	0.0029
353.15	0.0000	1.0000	0.0029
353.15	0.0068	0.0682	0.0006
353.15	0.0111	0.1152	0.0008
353.15	0.0135	0.0677	0.0006
353.15	0.0162	0.1759	0.0011
353.15	0.0202	0.0673	0.0007
353.15	0.0220	0.1139	0.0009
353.15	0.0267	0.0668	0.0007
353.15	0.0318	0.1728	0.0013
353.15	0.0326	0.1126	0.0009
353.15	0.0332	0.0664	0.0008
353.15	0.0430	0.1114	0.0011
353.15	0.0470	0.1699	0.0014
353.15	0.0531	0.1101	0.0013
353.15	0.0617	0.1671	0.0017
353.15	0.0759	0.1643	0.0019

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Viscosity, Pa*s - Liquid
0.2000	0.0070	0.0017
0.2000	0.0140	0.0019
0.2000	0.0200	0.0019
0.2000	0.0270	0.0021
0.2000	0.0330	0.0023
0.3000	0.0110	0.0025
0.3000	0.0220	0.0028
0.3000	0.0330	0.0032
0.3000	0.0430	0.0034
0.3000	0.0530	0.0040
0.4000	0.0160	0.0039
0.4000	0.0320	0.0047
0.4000	0.0470	0.0052
0.4000	0.0620	0.0059
0.4000	0.0760	0.0069

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Solvent: Mass fraction = 0.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0025
298.15	0.6900	0.0028
298.15	1.23	0.0030
298.15	1.87	0.0033
298.15	2.41	0.0037
303.15	0.0000	0.0022
303.15	0.6900	0.0024
303.15	1.23	0.0025
303.15	1.87	0.0028
303.15	2.41	0.0032
313.15	0.0000	0.0017
313.15	0.6900	0.0019
313.15	1.23	0.0019
313.15	1.87	0.0022
313.15	2.41	0.0025
323.15	0.0000	0.0013
323.15	0.6900	0.0015
323.15	1.23	0.0016
323.15	1.87	0.0017
323.15	2.41	0.0020
333.15	0.0000	0.0011
333.15	0.6900	0.0012
333.15	1.23	0.0013
333.15	1.87	0.0014
343.15	0.0000	0.0009
343.15	0.6900	0.0010
343.15	1.23	0.0011
353.15	0.0000	0.0008
353.15	0.6900	0.0009
353.15	1.23	0.0009

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Fixed		Measured
Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid	Mass ratio of solute to solvent of Water (3) - Liquid	Viscosity, Pa*s - Liquid
0.0000	4.0	0.0017
0.1500	4.0	0.0018
0.2500	4.0	0.0019
0.3500	4.0	0.0021
0.5000	4.0	0.0022
0.0000	2.333	0.0026
0.1500	2.333	0.0029
0.2500	2.333	0.0031
0.3500	2.333	0.0033
0.5000	2.333	0.0039
0.0000	1.5	0.0035
0.1500	1.5	0.0042
0.2500	1.5	0.0047
0.3500	1.5	0.0057
0.5000	1.5	0.0067

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0620	0.0000	293.15	0.0012
0.0620	0.0000	293.15	0.0012
0.0620	0.0000	303.15	0.0010
0.0620	0.0000	303.15	0.0010
0.0620	0.0000	313.15	0.0008
0.0620	0.0000	313.15	0.0008
0.0620	0.0000	323.15	0.0007
0.0620	0.0000	323.15	0.0007
0.0620	0.0000	333.15	0.0006
0.0620	0.0000	333.15	0.0006
0.0620	0.0068	293.15	0.0012
0.0620	0.0068	293.15	0.0012
0.0620	0.0068	303.15	0.0010
0.0620	0.0068	303.15	0.0010
0.0620	0.0068	313.15	0.0008
0.0620	0.0068	313.15	0.0008
0.0620	0.0068	323.15	0.0007
0.0620	0.0068	323.15	0.0007
0.0620	0.0068	333.15	0.0006
0.0620	0.0068	333.15	0.0006
0.0620	0.0091	293.15	0.0013
0.0620	0.0091	293.15	0.0013
0.0620	0.0091	303.15	0.0010
0.0620	0.0091	303.15	0.0010
0.0620	0.0091	313.15	0.0008
0.0620	0.0091	313.15	0.0008
0.0620	0.0091	323.15	0.0007
0.0620	0.0091	323.15	0.0007
0.0620	0.0091	333.15	0.0006
0.0620	0.0091	333.15	0.0006
0.3000	0.0000	293.15	0.0029
0.3000	0.0000	293.15	0.0029
0.3000	0.0000	298.15	0.0024
0.3000	0.0000	298.15	0.0025
0.3000	0.0000	303.15	0.0021
0.3000	0.0000	303.15	0.0021
0.3000	0.0000	313.15	0.0016
0.3000	0.0000	313.15	0.0016
0.3000	0.0000	323.15	0.0013
0.3000	0.0000	323.15	0.0013
0.3000	0.0000	333.15	0.0011
0.3000	0.0000	333.15	0.0011
0.3000	0.0000	343.15	0.0009
0.3000	0.0000	343.15	0.0009
0.3000	0.0000	353.15	0.0007
0.3000	0.0000	353.15	0.0007
0.3000	0.0130	293.15	0.0031
0.3000	0.0130	293.15	0.0031
0.3000	0.0130	298.15	0.0027
0.3000	0.0130	298.15	0.0026
0.3000	0.0130	303.15	0.0023
0.3000	0.0130	303.15	0.0023
0.3000	0.0130	313.15	0.0018
0.3000	0.0130	313.15	0.0018
0.3000	0.0130	323.15	0.0014
0.3000	0.0130	323.15	0.0014
0.3000	0.0130	333.15	0.0011
0.3000	0.0130	333.15	0.0011
0.3000	0.0130	343.15	0.0010
0.3000	0.0130	343.15	0.0010
0.3000	0.0130	353.15	0.0008
0.3000	0.0130	353.15	0.0008
0.3000	0.0215	293.15	0.0033
0.3000	0.0215	293.15	0.0033
0.3000	0.0215	298.15	0.0028
0.3000	0.0215	298.15	0.0028
0.3000	0.0215	303.15	0.0024
0.3000	0.0215	303.15	0.0024
0.3000	0.0215	313.15	0.0019
0.3000	0.0215	313.15	0.0019
0.3000	0.0215	323.15	0.0015
0.3000	0.0215	323.15	0.0015
0.3000	0.0215	333.15	0.0012
0.3000	0.0215	333.15	0.0012
0.3000	0.0215	343.15	0.0010
0.3000	0.0215	343.15	0.0010
0.3000	0.0215	353.15	0.0009
0.3000	0.0215	353.15	0.0009
0.3000	0.0328	293.15	0.0036
0.3000	0.0328	293.15	0.0036
0.3000	0.0328	298.15	0.0031
0.3000	0.0328	298.15	0.0031
0.3000	0.0328	303.15	0.0027
0.3000	0.0328	303.15	0.0027
0.3000	0.0328	313.15	0.0021
0.3000	0.0328	313.15	0.0021
0.3000	0.0328	323.15	0.0017
0.3000	0.0328	323.15	0.0017
0.3000	0.0328	333.15	0.0014
0.3000	0.0328	333.15	0.0014
0.3000	0.0328	343.15	0.0011
0.3000	0.0328	343.15	0.0012
0.3000	0.0328	353.15	0.0010
0.3000	0.0328	353.15	0.0010
0.3000	0.0431	293.15	0.0039
0.3000	0.0431	293.15	0.0039
0.3000	0.0431	298.15	0.0033
0.3000	0.0431	298.15	0.0033
0.3000	0.0431	303.15	0.0029
0.3000	0.0431	303.15	0.0029
0.3000	0.0431	313.15	0.0022
0.3000	0.0431	313.15	0.0022
0.3000	0.0431	323.15	0.0018
0.3000	0.0431	323.15	0.0018
0.3000	0.0431	333.15	0.0015
0.3000	0.0431	333.15	0.0015
0.3000	0.0431	343.15	0.0013
0.3000	0.0431	343.15	0.0013
0.3000	0.0431	353.15	0.0011
0.3000	0.0431	353.15	0.0011
0.3000	0.0544	293.15	0.0043
0.3000	0.0544	293.15	0.0043
0.3000	0.0544	298.15	0.0037
0.3000	0.0544	298.15	0.0037
0.3000	0.0544	303.15	0.0032
0.3000	0.0544	303.15	0.0032
0.3000	0.0544	313.15	0.0025
0.3000	0.0544	313.15	0.0025
0.3000	0.0544	323.15	0.0020
0.3000	0.0544	323.15	0.0020
0.3000	0.0544	333.15	0.0016
0.3000	0.0544	333.15	0.0016
0.3000	0.0544	343.15	0.0013
0.3000	0.0544	343.15	0.0014
0.3000	0.0544	353.15	0.0011
0.3000	0.0544	353.15	0.0011

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0687	0.0017
298.15	0.0000	0.1122	0.0025
298.15	0.0000	0.1643	0.0036
298.15	0.0000	0.2278	0.0055
298.15	0.0000	0.4076	0.0125
298.15	0.0000	0.7264	0.0194
298.15	0.0000	1.0000	0.0199
298.15	0.0068	0.0682	0.0018
298.15	0.0111	0.1152	0.0026
298.15	0.0135	0.0677	0.0019
298.15	0.0162	0.1759	0.0040
298.15	0.0202	0.0673	0.0019
298.15	0.0220	0.1139	0.0029
298.15	0.0267	0.0668	0.0021
298.15	0.0318	0.1728	0.0046
298.15	0.0326	0.1126	0.0031
298.15	0.0332	0.0664	0.0022
298.15	0.0430	0.1114	0.0035
298.15	0.0470	0.1699	0.0051
298.15	0.0531	0.1101	0.0039
298.15	0.0617	0.1671	0.0060
298.15	0.0759	0.1643	0.0070
313.15	0.0000	0.0687	0.0012
313.15	0.0000	0.1122	0.0017
313.15	0.0000	0.1643	0.0023
313.15	0.0000	0.2278	0.0034
313.15	0.0000	0.4076	0.0070
313.15	0.0000	0.7264	0.0102
313.15	0.0000	1.0000	0.0096
313.15	0.0068	0.0682	0.0013
313.15	0.0111	0.1152	0.0017
313.15	0.0135	0.0677	0.0013
313.15	0.0162	0.1759	0.0025
313.15	0.0202	0.0673	0.0013
313.15	0.0220	0.1139	0.0020
313.15	0.0267	0.0668	0.0014
313.15	0.0318	0.1728	0.0030
313.15	0.0326	0.1126	0.0020
313.15	0.0332	0.0664	0.0016
313.15	0.0430	0.1114	0.0024
313.15	0.0470	0.1699	0.0033
313.15	0.0531	0.1101	0.0027
313.15	0.0617	0.1671	0.0040
313.15	0.0759	0.1643	0.0046
323.15	0.0000	0.0687	0.0009
323.15	0.0000	0.1122	0.0013
323.15	0.0000	0.1643	0.0018
323.15	0.0000	0.2278	0.0025
323.15	0.0000	0.4076	0.0049
323.15	0.0000	0.7264	0.0071
323.15	0.0000	1.0000	0.0067
323.15	0.0068	0.0682	0.0010
323.15	0.0111	0.1152	0.0014
323.15	0.0135	0.0677	0.0010
323.15	0.0162	0.1759	0.0020
323.15	0.0202	0.0673	0.0011
323.15	0.0220	0.1139	0.0016
323.15	0.0267	0.0668	0.0012
323.15	0.0318	0.1728	0.0023
323.15	0.0326	0.1126	0.0016
323.15	0.0332	0.0664	0.0013
323.15	0.0430	0.1114	0.0019
323.15	0.0470	0.1699	0.0026
323.15	0.0531	0.1101	0.0021
323.15	0.0617	0.1671	0.0031
323.15	0.0759	0.1643	0.0038
343.15	0.0000	0.0687	0.0007
343.15	0.0000	0.1122	0.0009
343.15	0.0000	0.1643	0.0011
343.15	0.0000	0.2278	0.0016
343.15	0.0000	0.4076	0.0028
343.15	0.0000	0.7264	0.0038
343.15	0.0000	1.0000	0.0037
343.15	0.0068	0.0682	0.0007
343.15	0.0111	0.1152	0.0009
343.15	0.0135	0.0677	0.0007
343.15	0.0162	0.1759	0.0013
343.15	0.0202	0.0673	0.0008
343.15	0.0220	0.1139	0.0011
343.15	0.0267	0.0668	0.0008
343.15	0.0318	0.1728	0.0015
343.15	0.0326	0.1126	0.0011
343.15	0.0332	0.0664	0.0009
343.15	0.0430	0.1114	0.0013
343.15	0.0470	0.1699	0.0017
343.15	0.0531	0.1101	0.0015
343.15	0.0617	0.1671	0.0020
343.15	0.0759	0.1643	0.0023
353.15	0.0000	0.0687	0.0006
353.15	0.0000	0.1122	0.0008
353.15	0.0000	0.1643	0.0009
353.15	0.0000	0.2278	0.0013
353.15	0.0000	0.4076	0.0022
353.15	0.0000	0.7264	0.0029
353.15	0.0000	1.0000	0.0029
353.15	0.0068	0.0682	0.0006
353.15	0.0111	0.1152	0.0008
353.15	0.0135	0.0677	0.0006
353.15	0.0162	0.1759	0.0011
353.15	0.0202	0.0673	0.0007
353.15	0.0220	0.1139	0.0009
353.15	0.0267	0.0668	0.0007
353.15	0.0318	0.1728	0.0013
353.15	0.0326	0.1126	0.0009
353.15	0.0332	0.0664	0.0008
353.15	0.0430	0.1114	0.0011
353.15	0.0470	0.1699	0.0014
353.15	0.0531	0.1101	0.0013
353.15	0.0617	0.1671	0.0017
353.15	0.0759	0.1643	0.0019

Electrical conductivity, S/m [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Fixed		Measured
Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid	Mass ratio of solute to solvent of Water (3) - Liquid	Electrical conductivity, S/m - Liquid
0.0000	4.0	0.1020
0.1500	4.0	1.19
0.2500	4.0	1.804
0.3500	4.0	2.354
0.5000	4.0	3.08
0.0000	2.333	0.0720
0.1500	2.333	1.175
0.2500	2.333	1.771
0.3500	2.333	2.193
0.5000	2.333	2.74
0.0000	1.5	0.0460
0.1500	1.5	1.171
0.2500	1.5	1.68
0.3500	1.5	2.024
0.5000	1.5	2.333

Electrical conductivity, S/m [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Fixed		Measured
Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid	Mass ratio of solute to solvent of Water (3) - Liquid	Electrical conductivity, S/m - Liquid
0.0000	4.0	0.1020
0.1500	4.0	1.19
0.2500	4.0	1.804
0.3500	4.0	2.354
0.5000	4.0	3.08
0.0000	2.333	0.0720
0.1500	2.333	1.175
0.2500	2.333	1.771
0.3500	2.333	2.193
0.5000	2.333	2.74
0.0000	1.5	0.0460
0.1500	1.5	1.171
0.2500	1.5	1.68
0.3500	1.5	2.024
0.5000	1.5	2.333

Vapor or sublimation pressure, kPa [ref]

Fixed			Measured
Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Molality, mol/kg of Monoethanolamine (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
313.15	1.764	7.0	0.02
313.15	2.079	9.0	0.01
313.15	2.457	7.0	0.08
313.15	2.871	11.0	0.01
313.15	2.916	9.0	0.03
313.15	3.024	7.0	0.47
313.15	3.276	13.0	0.01
313.15	3.438	9.0	0.11
313.15	3.472	7.0	4.22
313.15	3.883	11.0	0.07
313.15	3.969	9.0	0.42
313.15	4.464	9.0	5.35
313.15	4.708	11.0	0.43
313.15	4.836	13.0	0.08
313.15	5.071	11.0	1.51
313.15	5.655	13.0	0.49
313.15	6.526	13.0	8.79
333.15	1.764	7.0	0.11
333.15	2.079	9.0	0.06
333.15	2.457	7.0	0.66
333.15	2.871	11.0	0.10
333.15	2.916	9.0	0.26
333.15	3.024	7.0	3.43
333.15	3.276	13.0	0.10
333.15	3.438	9.0	0.89
333.15	3.472	7.0	16.16
333.15	3.883	11.0	0.63
333.15	3.969	9.0	2.86
333.15	4.464	9.0	21.25
333.15	4.708	11.0	3.46
333.15	4.836	13.0	0.69
333.15	5.071	11.0	8.17
333.15	5.655	13.0	3.86
333.15	6.526	13.0	29.43
353.15	1.897	7.0	1.05
353.15	2.385	9.0	0.98
353.15	2.562	7.0	4.44
353.15	2.816	11.0	0.86
353.15	3.204	9.0	4.80
353.15	3.302	13.0	0.87
353.15	3.949	11.0	3.92
353.15	4.615	13.0	3.96
373.10	1.897	7.0	5.30
373.10	2.385	9.0	4.94
373.10	2.562	7.0	19.01
373.10	2.816	11.0	4.27
373.10	3.204	9.0	21.53
373.10	3.302	13.0	3.88
373.10	3.949	11.0	18.66
373.10	4.615	13.0	18.41

Vapor or sublimation pressure, kPa [ref]

Fixed			Measured
Temperature, K - Liquid	Molality, mol/kg of Monoethanolamine (1) - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
313.63	2.856	2.863	1813.00
313.27	2.911	2.962	2134.00
313.22	2.911	3.125	2770.00
313.21	2.911	3.216	3450.00
313.11	2.889	3.541	5240.00
313.20	2.931	3.76	8070.00
353.14	2.93	2.111	803.00
353.23	2.93	2.156	970.00
353.15	2.93	2.244	1198.00
353.18	2.93	2.374	1623.00
353.19	2.93	2.548	2400.00
353.20	2.93	2.665	3100.00
353.24	2.93	2.732	3470.00
353.20	2.93	2.836	4340.00
353.17	2.93	2.899	4750.00
353.23	2.93	3.08	6350.00
393.11	2.856	1.518	786.00
393.16	2.856	1.72	1359.00
393.15	2.856	1.894	2111.00
393.14	2.856	1.992	2490.00
393.15	2.856	2.087	3300.00
393.17	2.856	2.17	3650.00
393.15	2.856	2.308	4670.00
393.15	2.856	2.425	5440.00
393.16	2.856	2.52	6580.00
393.16	2.856	2.699	8740.00
313.23	7.008	4.98	448.00
313.24	7.008	5.267	695.00
313.24	7.008	5.261	739.00
313.18	7.069	5.405	745.00
313.23	7.008	5.739	1312.00
313.26	7.008	5.965	1671.00
313.24	7.008	6.627	3620.00
313.23	7.008	6.855	4920.00
313.25	7.008	7.233	7320.00
313.20	7.008	7.279	7510.00
353.26	7.069	4.151	513.00
353.16	7.069	4.544	981.00
353.17	7.069	4.862	1715.00
353.18	7.069	5.027	2234.00
353.16	7.069	5.182	2710.00
353.15	7.069	5.457	3800.00
353.21	7.069	5.732	5520.00
353.18	7.069	6.059	7400.00
393.14	7.069	3.37	644.00
393.19	7.069	3.603	972.00
393.19	7.069	3.731	1249.00
393.19	7.069	3.995	2084.00
393.21	7.069	4.148	2760.00
393.18	7.069	4.255	3230.00
393.19	7.069	4.316	3410.00
393.21	7.069	4.483	4210.00
393.19	7.069	4.709	5230.00
393.16	7.069	4.987	7230.00

Vapor or sublimation pressure, kPa [ref]

Fixed			Measured
Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Molality, mol/kg of Monoethanolamine (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
313.15	1.764	7.0	0.02
313.15	2.079	9.0	0.01
313.15	2.457	7.0	0.08
313.15	2.871	11.0	0.01
313.15	2.916	9.0	0.03
313.15	3.024	7.0	0.47
313.15	3.276	13.0	0.01
313.15	3.438	9.0	0.11
313.15	3.472	7.0	4.22
313.15	3.883	11.0	0.07
313.15	3.969	9.0	0.42
313.15	4.464	9.0	5.35
313.15	4.708	11.0	0.43
313.15	4.836	13.0	0.08
313.15	5.071	11.0	1.51
313.15	5.655	13.0	0.49
313.15	6.526	13.0	8.79
333.15	1.764	7.0	0.11
333.15	2.079	9.0	0.06
333.15	2.457	7.0	0.66
333.15	2.871	11.0	0.10
333.15	2.916	9.0	0.26
333.15	3.024	7.0	3.43
333.15	3.276	13.0	0.10
333.15	3.438	9.0	0.89
333.15	3.472	7.0	16.16
333.15	3.883	11.0	0.63
333.15	3.969	9.0	2.86
333.15	4.464	9.0	21.25
333.15	4.708	11.0	3.46
333.15	4.836	13.0	0.69
333.15	5.071	11.0	8.17
333.15	5.655	13.0	3.86
333.15	6.526	13.0	29.43
353.15	1.897	7.0	1.05
353.15	2.385	9.0	0.98
353.15	2.562	7.0	4.44
353.15	2.816	11.0	0.86
353.15	3.204	9.0	4.80
353.15	3.302	13.0	0.87
353.15	3.949	11.0	3.92
353.15	4.615	13.0	3.96
373.10	1.897	7.0	5.30
373.10	2.385	9.0	4.94
373.10	2.562	7.0	19.01
373.10	2.816	11.0	4.27
373.10	3.204	9.0	21.53
373.10	3.302	13.0	3.88
373.10	3.949	11.0	18.66
373.10	4.615	13.0	18.41

Vapor or sublimation pressure, kPa [ref]

Fixed			Measured
Temperature, K - Liquid	Molality, mol/kg of Monoethanolamine (1) - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
313.63	2.856	2.863	1813.00
313.27	2.911	2.962	2134.00
313.22	2.911	3.125	2770.00
313.21	2.911	3.216	3450.00
313.11	2.889	3.541	5240.00
313.20	2.931	3.76	8070.00
353.14	2.93	2.111	803.00
353.23	2.93	2.156	970.00
353.15	2.93	2.244	1198.00
353.18	2.93	2.374	1623.00
353.19	2.93	2.548	2400.00
353.20	2.93	2.665	3100.00
353.24	2.93	2.732	3470.00
353.20	2.93	2.836	4340.00
353.17	2.93	2.899	4750.00
353.23	2.93	3.08	6350.00
393.11	2.856	1.518	786.00
393.16	2.856	1.72	1359.00
393.15	2.856	1.894	2111.00
393.14	2.856	1.992	2490.00
393.15	2.856	2.087	3300.00
393.17	2.856	2.17	3650.00
393.15	2.856	2.308	4670.00
393.15	2.856	2.425	5440.00
393.16	2.856	2.52	6580.00
393.16	2.856	2.699	8740.00
313.23	7.008	4.98	448.00
313.24	7.008	5.267	695.00
313.24	7.008	5.261	739.00
313.18	7.069	5.405	745.00
313.23	7.008	5.739	1312.00
313.26	7.008	5.965	1671.00
313.24	7.008	6.627	3620.00
313.23	7.008	6.855	4920.00
313.25	7.008	7.233	7320.00
313.20	7.008	7.279	7510.00
353.26	7.069	4.151	513.00
353.16	7.069	4.544	981.00
353.17	7.069	4.862	1715.00
353.18	7.069	5.027	2234.00
353.16	7.069	5.182	2710.00
353.15	7.069	5.457	3800.00
353.21	7.069	5.732	5520.00
353.18	7.069	6.059	7400.00
393.14	7.069	3.37	644.00
393.19	7.069	3.603	972.00
393.19	7.069	3.731	1249.00
393.19	7.069	3.995	2084.00
393.21	7.069	4.148	2760.00
393.18	7.069	4.255	3230.00
393.19	7.069	4.316	3410.00
393.21	7.069	4.483	4210.00
393.19	7.069	4.709	5230.00
393.16	7.069	4.987	7230.00

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Fixed		Measured
Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid	Mass ratio of solute to solvent of Water (3) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	4.0	1.3587
0.1500	4.0	1.3642
0.2500	4.0	1.3676
0.3500	4.0	1.3709
0.5000	4.0	1.3752
0.0000	2.333	1.372
0.1500	2.333	1.3809
0.2500	2.333	1.3863
0.3500	2.333	1.3913
0.5000	2.333	1.3978
0.0000	1.5	1.3854
0.1500	1.5	1.396
0.2500	1.5	1.4029
0.3500	1.5	1.4101
0.5000	1.5	1.418

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Fixed		Measured
Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid	Mass ratio of solute to solvent of Water (3) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	4.0	1.3587
0.1500	4.0	1.3642
0.2500	4.0	1.3676
0.3500	4.0	1.3709
0.5000	4.0	1.3752
0.0000	2.333	1.372
0.1500	2.333	1.3809
0.2500	2.333	1.3863
0.3500	2.333	1.3913
0.5000	2.333	1.3978
0.0000	1.5	1.3854
0.1500	1.5	1.396
0.2500	1.5	1.4029
0.3500	1.5	1.4101
0.5000	1.5	1.418

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Solvent: Mass fraction = 0.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	1010.44
298.15	0.6900	1041.76
298.15	1.23	1066.68
298.15	1.87	1093.32
298.15	2.41	1117.07
299.15	0.0000	1010.01
299.15	0.6900	1041.33
299.15	1.23	1066.14
299.15	1.87	1092.89
299.15	2.41	1116.59
301.15	0.0000	1009.11
301.15	0.6900	1040.44
301.15	1.23	1065.14
301.15	1.87	1091.99
301.15	2.41	1115.64
303.15	0.0000	1008.2
303.15	0.6900	1039.54
303.15	1.23	1064.06
303.15	1.87	1091.07
303.15	2.41	1114.68
313.15	0.0000	1003.32
313.15	0.6900	1034.74
313.15	1.23	1058.86
313.15	1.87	1086.19
313.15	2.41	1109.69
323.15	0.0000	997.9
323.15	0.6900	1029.53
323.15	1.23	1053.28
323.15	1.87	1081.03
323.15	2.41	1104.41
333.15	0.0000	992.21
333.15	0.6900	1023.93
333.15	1.23	1047.69
333.15	1.87	1075.51
343.15	0.0000	985.83
343.15	0.6900	1017.95
343.15	1.23	1041.82
343.15	1.87	1069.66
353.15	0.0000	979.22
353.15	0.6900	1011.44
353.15	1.23	1035.47
353.15	1.87	1063.49

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Fixed		Measured
Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid	Mass ratio of solute to solvent of Water (3) - Liquid	Mass density, kg/m3 - Liquid
0.0000	4.0	1007.1
0.1500	4.0	1029.0
0.2500	4.0	1045.9
0.3500	4.0	1059.0
0.5000	4.0	1081.0
0.0000	2.333	1012.9
0.1500	2.333	1044.2
0.2500	2.333	1065.0
0.3500	2.333	1085.1
0.5000	2.333	1105.0
0.0000	1.5	1018.3
0.1500	1.5	1058.9
0.2500	1.5	1086.6
0.3500	1.5	1112.3
0.5000	1.5	1138.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0091	0.1112	1037.6
298.15	0.0111	0.1110	1033.3
298.15	0.0113	0.1109	1054.4
298.15	0.0135	0.1107	1065.3
298.15	0.0188	0.1101	1062.7
298.15	0.0230	0.1096	1053.4
298.15	0.0245	0.1095	1090.5
298.15	0.0293	0.1089	1094.5
298.15	0.0347	0.1083	1075.6
298.15	0.0374	0.1080	1130.8
298.15	0.0395	0.1078	1129.6
298.15	0.0445	0.1072	1153.6
298.15	0.0471	0.1069	1096.4
298.15	0.0510	0.1065	1166.8
298.15	0.0591	0.1056	1114.2
298.15	0.0617	0.1053	1200.2
298.15	0.0293	0.1089	1099.3
313.15	0.0091	0.1112	1029.5
313.15	0.0111	0.1110	1025.3
313.15	0.0113	0.1109	1044.8
313.15	0.0135	0.1107	1055.4
313.15	0.0188	0.1101	1054.7
313.15	0.0230	0.1096	1046.4
313.15	0.0245	0.1095	1081.7
313.15	0.0293	0.1089	1086.7
313.15	0.0347	0.1083	1066.9
313.15	0.0374	0.1080	1122.5
313.15	0.0395	0.1078	1119.9
313.15	0.0445	0.1072	1145.0
313.15	0.0471	0.1069	1089.1
313.15	0.0510	0.1065	1158.5
313.15	0.0591	0.1056	1106.8
313.15	0.0617	0.1053	1191.6
313.15	0.0293	0.1089	1088.9
323.15	0.0091	0.1112	1023.7
323.15	0.0111	0.1110	1019.6
323.15	0.0113	0.1109	1038.4
323.15	0.0135	0.1107	1048.9
323.15	0.0188	0.1101	1049.0
323.15	0.0230	0.1096	1041.2
323.15	0.0245	0.1095	1075.7
323.15	0.0293	0.1089	1081.1
323.15	0.0347	0.1083	1061.3
323.15	0.0374	0.1080	1116.8
323.15	0.0395	0.1078	1113.8
323.15	0.0445	0.1072	1139.1
323.15	0.0471	0.1069	1083.8
323.15	0.0510	0.1065	1152.8
323.15	0.0591	0.1056	1101.4
323.15	0.0617	0.1053	1185.8
323.15	0.0293	0.1089	1081.7
333.15	0.0091	0.1112	1017.8
333.15	0.0111	0.1110	1013.8
333.15	0.0113	0.1109	1032.0
333.15	0.0135	0.1107	1042.1
333.15	0.0188	0.1101	1043.0
333.15	0.0230	0.1096	1035.6
333.15	0.0245	0.1095	1069.7
333.15	0.0293	0.1089	1074.4
333.15	0.0347	0.1083	1055.6
333.15	0.0374	0.1080	1110.8
333.15	0.0395	0.1078	1108.7
333.15	0.0445	0.1072	1133.1
333.15	0.0471	0.1069	1078.2
333.15	0.0510	0.1065	1146.9
333.15	0.0591	0.1056	1095.7
333.15	0.0617	0.1053	1179.8
333.15	0.0293	0.1089	1075.2
343.15	0.0091	0.1112	1011.0
343.15	0.0111	0.1110	1007.6
343.15	0.0113	0.1109	1025.2
343.15	0.0135	0.1107	1035.1
343.15	0.0188	0.1101	1036.7
343.15	0.0230	0.1096	1029.7
343.15	0.0245	0.1095	1063.2
343.15	0.0293	0.1089	1066.6
343.15	0.0347	0.1083	1049.6
343.15	0.0374	0.1080	1104.8
343.15	0.0395	0.1078	1103.2
343.15	0.0445	0.1072	1127.0
343.15	0.0471	0.1069	1072.3
343.15	0.0510	0.1065	1140.8
343.15	0.0591	0.1056	1088.7
343.15	0.0617	0.1053	1173.7
343.15	0.0293	0.1089	1068.6
353.15	0.0091	0.1112	1004.8
353.15	0.0111	0.1110	1000.2
353.15	0.0113	0.1109	1018.3
353.15	0.0135	0.1107	1028.0
353.15	0.0188	0.1101	1029.2
353.15	0.0230	0.1096	1023.4
353.15	0.0245	0.1095	1056.7
353.15	0.0293	0.1089	1062.6
353.15	0.0347	0.1083	1043.4
353.15	0.0374	0.1080	1098.5
353.15	0.0395	0.1078	1096.3
353.15	0.0445	0.1072	1120.7
353.15	0.0471	0.1069	1066.0
353.15	0.0510	0.1065	1134.5
353.15	0.0591	0.1056	1081.2
353.15	0.0617	0.1053	1167.8
353.15	0.0293	0.1089	1058.0
363.15	0.0091	0.1112	997.0
363.15	0.0111	0.1110	993.6
363.15	0.0113	0.1109	1011.0
363.15	0.0135	0.1107	1020.6
363.15	0.0188	0.1101	1023.2
363.15	0.0230	0.1096	1016.7
363.15	0.0245	0.1095	1049.9
363.15	0.0293	0.1089	1049.4
363.15	0.0347	0.1083	1036.7
363.15	0.0374	0.1080	1092.0
363.15	0.0395	0.1078	1088.8
363.15	0.0445	0.1072	1114.3
363.15	0.0471	0.1069	1059.5
363.15	0.0510	0.1065	1127.3
363.15	0.0591	0.1056	1074.9
363.15	0.0617	0.1053	1160.6
363.15	0.0293	0.1089	1055.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 700 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mass density, kg/m3 - Liquid
373.10	0.0091	0.1112	990.5
373.10	0.0111	0.1110	986.5
373.10	0.0113	0.1109	1004.5
373.10	0.0135	0.1107	1014.5
373.10	0.0188	0.1101	1016.2
373.10	0.0230	0.1096	1009.2
373.10	0.0245	0.1095	1043.0
373.10	0.0293	0.1089	1049.4
373.10	0.0347	0.1083	1030.6
373.10	0.0374	0.1080	1085.4
373.10	0.0395	0.1078	1082.4
373.10	0.0445	0.1072	1107.0
373.10	0.0471	0.1069	1054.5
373.10	0.0510	0.1065	1119.6
373.10	0.0591	0.1056	1069.1
373.10	0.0617	0.1053	1153.7
373.10	0.0293	0.1089	1042.3
383.15	0.0091	0.1112	983.1
383.15	0.0111	0.1110	980.1
383.15	0.0113	0.1109	997.5
383.15	0.0135	0.1107	1007.3
383.15	0.0188	0.1101	1009.2
383.15	0.0230	0.1096	1002.3
383.15	0.0245	0.1095	1036.9
383.15	0.0293	0.1089	1043.9
383.15	0.0347	0.1083	1024.2
383.15	0.0374	0.1080	1079.7
383.15	0.0395	0.1078	1076.6
383.15	0.0445	0.1072	1098.3
383.15	0.0471	0.1069	1048.2
383.15	0.0510	0.1065	1112.5
383.15	0.0591	0.1056	1063.3
383.15	0.0617	0.1053	1147.8
383.15	0.0293	0.1089	1035.3
393.15	0.0091	0.1112	975.7
393.15	0.0111	0.1110	973.7
393.15	0.0113	0.1109	990.8
393.15	0.0135	0.1107	1000.7
393.15	0.0188	0.1101	1002.3
393.15	0.0230	0.1096	995.7
393.15	0.0245	0.1095	1028.8
393.15	0.0293	0.1089	1036.7
393.15	0.0347	0.1083	1018.3
393.15	0.0374	0.1080	1073.9
393.15	0.0395	0.1078	1069.9
393.15	0.0445	0.1072	1092.2
393.15	0.0471	0.1069	1041.7
393.15	0.0510	0.1065	1104.8
393.15	0.0591	0.1056	1057.6
393.15	0.0617	0.1053	1141.3
393.15	0.0293	0.1089	1028.9
403.15	0.0091	0.1112	967.8
403.15	0.0111	0.1110	967.4
403.15	0.0113	0.1109	983.3
403.15	0.0135	0.1107	994.9
403.15	0.0188	0.1101	994.6
403.15	0.0230	0.1096	988.9
403.15	0.0245	0.1095	1021.0
403.15	0.0293	0.1089	1029.8
403.15	0.0347	0.1083	1012.9
403.15	0.0374	0.1080	1067.9
403.15	0.0395	0.1078	1063.1
403.15	0.0445	0.1072	1085.7
403.15	0.0471	0.1069	1036.1
403.15	0.0510	0.1065	1098.4
403.15	0.0591	0.1056	1051.9
403.15	0.0617	0.1053	1136.3
403.15	0.0293	0.1089	1022.3
413.15	0.0091	0.1112	960.5
413.15	0.0111	0.1110	960.5
413.15	0.0113	0.1109	976.8
413.15	0.0135	0.1107	989.6
413.15	0.0188	0.1101	987.6
413.15	0.0230	0.1096	982.6
413.15	0.0245	0.1095	1012.8
413.15	0.0293	0.1089	1023.3
413.15	0.0347	0.1083	1007.9
413.15	0.0374	0.1080	1061.2
413.15	0.0395	0.1078	1057.5
413.15	0.0445	0.1072	1079.5
413.15	0.0471	0.1069	1029.5
413.15	0.0510	0.1065	1092.6
413.15	0.0591	0.1056	1045.6
413.15	0.0617	0.1053	1130.4
413.15	0.0293	0.1089	1017.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mass density, kg/m3 - Liquid
313.15	0.4241	0.2163	1240.9
313.15	0.4278	0.2096	1232.1
313.15	0.4296	0.2062	1232.5
313.15	0.4314	0.2028	1223.4
313.15	0.4333	0.1993	1220.8
313.15	0.4371	0.1923	1216.4
313.15	0.4410	0.1852	1209.0
313.15	0.4449	0.1780	1197.2
313.15	0.4489	0.1706	1189.9
313.15	0.4509	0.1668	1181.5
313.15	0.4550	0.1593	1173.3
313.15	0.4634	0.1437	1158.2
313.15	0.4656	0.1397	1154.0
313.15	0.4678	0.1357	1154.0
313.15	0.4700	0.1316	1148.6
313.15	0.4860	0.1021	1115.0
313.15	0.5214	0.0365	1053.4
313.15	0.4489	0.1706	1188.7
313.15	0.4656	0.1397	1152.0
313.15	0.4860	0.1021	1114.8
313.15	0.4860	0.1021	1117.6
323.15	0.4259	0.2130	1232.3
323.15	0.4278	0.2096	1226.6
323.15	0.4296	0.2062	1226.1
323.15	0.4314	0.2028	1217.1
323.15	0.4333	0.1993	1213.8
323.15	0.4371	0.1923	1210.8
323.15	0.4410	0.1852	1203.7
323.15	0.4449	0.1780	1191.8
323.15	0.4489	0.1706	1184.5
323.15	0.4509	0.1668	1176.0
323.15	0.4550	0.1593	1167.8
323.15	0.4634	0.1437	1150.9
323.15	0.4656	0.1397	1148.2
323.15	0.4678	0.1357	1148.2
323.15	0.4700	0.1316	1142.9
323.15	0.4836	0.1064	1111.1
323.15	0.4860	0.1021	1108.5
323.15	0.5214	0.0365	1046.3
323.15	0.4489	0.1706	1183.0
323.15	0.4656	0.1397	1146.5
323.15	0.4860	0.1021	1108.7
333.15	0.4259	0.2130	1223.9
333.15	0.4278	0.2096	1220.9
333.15	0.4352	0.1958	1207.8
333.15	0.4390	0.1888	1205.2
333.15	0.4410	0.1852	1198.2
333.15	0.4449	0.1780	1185.5
333.15	0.4489	0.1706	1177.3
333.15	0.4509	0.1668	1168.8
333.15	0.4550	0.1593	1161.8
333.15	0.4634	0.1437	1143.6
333.15	0.4656	0.1397	1140.2
333.15	0.4678	0.1357	1135.8
333.15	0.4836	0.1064	1104.5
333.15	0.4860	0.1021	1102.6
333.15	0.5214	0.0365	1039.1
333.15	0.4509	0.1668	1179.3
333.15	0.4678	0.1357	1139.7
333.15	0.4860	0.1021	1101.4
343.15	0.4278	0.2096	1215.1
343.15	0.4352	0.1958	1198.8
343.15	0.4390	0.1888	1198.8
343.15	0.4410	0.1852	1192.3
343.15	0.4449	0.1780	1179.9
343.15	0.4489	0.1706	1174.0
343.15	0.4509	0.1668	1163.6
343.15	0.4550	0.1593	1156.6
343.15	0.4634	0.1437	1138.5
343.15	0.4656	0.1397	1135.0
343.15	0.4678	0.1357	1130.4
343.15	0.4836	0.1064	1098.8
343.15	0.4860	0.1021	1096.7
343.15	0.5214	0.0365	1031.8
343.15	0.4489	0.1706	1171.5
343.15	0.4656	0.1397	1134.5
343.15	0.4860	0.1021	1095.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 800 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0687	0.0000	1003.6
303.15	0.0682	0.0068	1019.1
303.15	0.0677	0.0135	1032.4
303.15	0.0673	0.0202	1046.7
303.15	0.0668	0.0267	1061.1
303.15	0.0664	0.0332	1074.4
313.15	0.0687	0.0000	999.4
313.15	0.0682	0.0068	1014.8
313.15	0.0677	0.0135	1028.1
313.15	0.0673	0.0202	1042.4
313.15	0.0668	0.0267	1056.7
313.15	0.0664	0.0332	1069.8
323.15	0.0687	0.0000	994.6
323.15	0.0682	0.0068	1010.2
323.15	0.0677	0.0135	1023.3
323.15	0.0673	0.0202	1037.6
323.15	0.0668	0.0267	1051.8
323.15	0.0664	0.0332	1064.9
333.15	0.0687	0.0000	989.1
333.15	0.0682	0.0068	1004.8
333.15	0.0677	0.0135	1018.0
333.15	0.0673	0.0202	1032.3
333.15	0.0668	0.0267	1046.4
333.15	0.0664	0.0332	1059.4
303.15	0.1122	0.0000	1008.2
303.15	0.1110	0.0111	1027.8
303.15	0.1097	0.0219	1047.5
303.15	0.1085	0.0326	1066.1
303.15	0.1074	0.0430	1086.3
303.15	0.1062	0.0531	1106.0
313.15	0.1122	0.0000	1003.3
313.15	0.1110	0.0111	1022.9
313.15	0.1097	0.0219	1042.7
313.15	0.1085	0.0326	1061.4
313.15	0.1074	0.0430	1081.5
313.15	0.1062	0.0531	1101.0
323.15	0.1122	0.0000	998.1
323.15	0.1110	0.0111	1017.8
323.15	0.1097	0.0219	1037.6
323.15	0.1085	0.0326	1056.3
323.15	0.1074	0.0430	1076.3
323.15	0.1062	0.0531	1095.8
333.15	0.1122	0.0000	992.3
333.15	0.1110	0.0111	1012.0
333.15	0.1097	0.0219	1032.0
333.15	0.1085	0.0326	1050.7
333.15	0.1074	0.0430	1070.7
333.15	0.1062	0.0531	1090.1
303.15	0.1643	0.0000	1013.3
303.15	0.1616	0.0162	1037.8
303.15	0.1591	0.0318	1062.8
303.15	0.1566	0.0470	1087.6
303.15	0.1542	0.0617	1113.9
303.15	0.1518	0.0759	1139.6
313.15	0.1643	0.0000	1007.8
313.15	0.1616	0.0162	1032.5
313.15	0.1591	0.0318	1057.6
313.15	0.1566	0.0470	1082.5
313.15	0.1542	0.0617	1108.6
313.15	0.1518	0.0759	1134.4
323.15	0.1643	0.0000	1002.1
323.15	0.1616	0.0162	1026.9
323.15	0.1591	0.0318	1052.1
323.15	0.1566	0.0470	1077.1
323.15	0.1542	0.0617	1103.2
323.15	0.1518	0.0759	1129.0
333.15	0.1643	0.0000	995.7
333.15	0.1616	0.0162	1020.8
333.15	0.1591	0.0318	1046.2
333.15	0.1566	0.0470	1071.3
333.15	0.1542	0.0617	1097.5
333.15	0.1518	0.0759	1123.2
303.15	0.2277	0.0000	1017.8
303.15	0.2227	0.0223	1047.2
303.15	0.2178	0.0436	1075.1
303.15	0.2132	0.0640	1106.7
303.15	0.2087	0.0835	1136.4
303.15	0.2045	0.1022	1167.7
313.15	0.2277	0.0000	1011.8
313.15	0.2227	0.0223	1040.6
313.15	0.2178	0.0436	1069.4
313.15	0.2132	0.0640	1099.9
313.15	0.2087	0.0835	1131.0
313.15	0.2045	0.1022	1162.1
323.15	0.2277	0.0000	1005.4
323.15	0.2227	0.0223	1034.4
323.15	0.2178	0.0436	1063.6
323.15	0.2132	0.0640	1093.9
323.15	0.2087	0.0835	1125.4
323.15	0.2045	0.1022	1156.5
333.15	0.2277	0.0000	998.7
333.15	0.2227	0.0223	1027.9
333.15	0.2178	0.0436	1057.4
333.15	0.2132	0.0640	1088.0
333.15	0.2087	0.0835	1119.6
333.15	0.2045	0.1022	1150.7
303.15	0.3067	0.0000	1021.3
303.15	0.2976	0.0298	1058.6
303.15	0.2890	0.0578	1091.6
303.15	0.2808	0.0843	1126.2
303.15	0.2732	0.1093	1162.1
303.15	0.2659	0.1330	1197.6
313.15	0.3067	0.0000	1014.6
313.15	0.2976	0.0298	1052.3
313.15	0.2890	0.0578	1085.6
313.15	0.2808	0.0843	1120.4
313.15	0.2732	0.1093	1156.5
313.15	0.2659	0.1330	1192.0
323.15	0.3067	0.0000	1007.8
323.15	0.2976	0.0298	1045.9
323.15	0.2890	0.0578	1079.5
323.15	0.2808	0.0843	1114.6
323.15	0.2732	0.1093	1150.8
323.15	0.2659	0.1330	1186.3
333.15	0.3067	0.0000	1000.6
333.15	0.2976	0.0298	1039.2
333.15	0.2890	0.0578	1073.1
333.15	0.2808	0.0843	1108.5
333.15	0.2732	0.1093	1144.9
333.15	0.2659	0.1330	1180.4
303.15	0.4076	0.0000	1022.6
303.15	0.3916	0.0392	1063.9
303.15	0.3769	0.0754	1101.1
303.15	0.3632	0.1090	1143.7
303.15	0.3505	0.1402	1185.4
303.15	0.3386	0.1693	1226.2
313.15	0.4076	0.0000	1015.5
313.15	0.3916	0.0392	1057.3
313.15	0.3769	0.0754	1094.8
313.15	0.3632	0.1090	1137.8
313.15	0.3505	0.1402	1179.7
313.15	0.3386	0.1693	1220.4
323.15	0.4076	0.0000	1008.2
323.15	0.3916	0.0392	1050.6
323.15	0.3769	0.0754	1088.4
323.15	0.3632	0.1090	1131.8
323.15	0.3505	0.1402	1174.0
323.15	0.3386	0.1693	1214.7
333.15	0.4076	0.0000	1000.6
333.15	0.3916	0.0392	1043.6
333.15	0.3769	0.0754	1081.9
333.15	0.3632	0.1090	1125.6
333.15	0.3505	0.1402	1168.1
333.15	0.3386	0.1693	1208.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0620	0.0000	293.15	1000.88
0.0620	0.0000	303.15	998.06
0.0620	0.0000	313.15	994.42
0.0620	0.0000	323.15	990.09
0.0620	0.0000	333.15	985.12
0.0620	0.0000	343.15	978.86
0.0620	0.0000	353.15	973.57
0.0620	0.0019	293.15	1004.95
0.0620	0.0019	303.15	1002.16
0.0620	0.0019	313.15	998.47
0.0620	0.0019	323.15	994.07
0.0620	0.0019	333.15	989.1
0.0620	0.0019	343.15	983.58
0.0620	0.0019	353.15	977.56
0.0620	0.0037	293.15	1009.77
0.0620	0.0037	303.15	1006.8
0.0620	0.0037	313.15	1003.09
0.0620	0.0037	323.15	998.72
0.0620	0.0037	333.15	993.75
0.0620	0.0037	343.15	988.22
0.0620	0.0037	353.15	981.76
0.0620	0.0068	293.15	1017.47
0.0620	0.0068	303.15	1014.52
0.0620	0.0068	313.15	1010.79
0.0620	0.0068	323.15	1006.21
0.0620	0.0068	333.15	1001.33
0.0620	0.0068	343.15	995.87
0.0620	0.0068	353.15	989.89
0.0620	0.0089	293.15	1022.17
0.0620	0.0089	303.15	1019.0
0.0620	0.0089	313.15	1015.13
0.0620	0.0089	323.15	1010.67
0.0620	0.0089	333.15	1005.6
0.0620	0.0089	343.15	1000.03
0.0620	0.0089	353.15	993.98
0.3000	0.0000	293.15	1012.68
0.3000	0.0000	298.15	1010.55
0.3000	0.0000	303.15	1008.31
0.3000	0.0000	313.15	1003.45
0.3000	0.0000	323.15	998.07
0.3000	0.0000	333.15	992.23
0.3000	0.0000	343.15	985.96
0.3000	0.0000	353.15	979.27
0.3000	0.0130	293.15	1030.99
0.3000	0.0130	298.15	1028.87
0.3000	0.0130	303.15	1026.65
0.3000	0.0130	313.15	1021.88
0.3000	0.0130	323.15	1016.6
0.3000	0.0130	333.15	1010.9
0.3000	0.0130	343.15	1004.8
0.3000	0.0130	353.15	998.31
0.3000	0.0215	293.15	1046.92
0.3000	0.0215	298.15	1044.8
0.3000	0.0215	303.15	1042.58
0.3000	0.0215	313.15	1037.84
0.3000	0.0215	323.15	1032.62
0.3000	0.0215	333.15	1027.0
0.3000	0.0215	343.15	1021.01
0.3000	0.0215	353.15	1014.66
0.3000	0.0328	293.15	1068.9
0.3000	0.0328	298.15	1066.76
0.3000	0.0328	303.15	1064.53
0.3000	0.0328	313.15	1059.81
0.3000	0.0328	323.15	1054.64
0.3000	0.0328	333.15	1049.12
0.3000	0.0328	343.15	1043.23
0.3000	0.0328	353.15	1037.04
0.3000	0.0431	293.15	1086.89
0.3000	0.0431	298.15	1084.7
0.3000	0.0431	303.15	1082.44
0.3000	0.0431	313.15	1077.75
0.3000	0.0431	323.15	1072.6
0.3000	0.0431	333.15	1067.11
0.3000	0.0431	343.15	1061.28
0.3000	0.0431	353.15	1055.16
0.3000	0.0544	293.15	1108.2
0.3000	0.0544	298.15	1105.88
0.3000	0.0544	303.15	1103.51
0.3000	0.0544	313.15	1098.66
0.3000	0.0544	323.15	1093.45
0.3000	0.0544	333.15	1087.88
0.3000	0.0544	343.15	1082.0
0.3000	0.0544	353.15	1075.85

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	0.0687	1005.0
298.15	0.0000	0.1122	1011.0
298.15	0.0000	0.1643	1016.0
298.15	0.0000	0.2278	1021.0
298.15	0.0000	0.4076	1026.0
298.15	0.0000	0.7264	1020.0
298.15	0.0000	1.0000	1012.0
298.15	0.0068	0.0682	1019.0
298.15	0.0111	0.1152	1028.0
298.15	0.0135	0.0677	1033.0
298.15	0.0162	0.1759	1038.0
298.15	0.0202	0.0673	1048.0
298.15	0.0220	0.1139	1048.0
298.15	0.0267	0.0668	1064.0
298.15	0.0318	0.1728	1063.0
298.15	0.0326	0.1126	1070.0
298.15	0.0332	0.0664	1080.0
298.15	0.0430	0.1114	1096.0
298.15	0.0470	0.1699	1093.0
298.15	0.0531	0.1101	1121.0
298.15	0.0617	0.1671	1129.0
298.15	0.0759	0.1643	1160.0
313.15	0.0000	0.0687	999.0
313.15	0.0000	0.1122	1003.0
313.15	0.0000	0.1643	1008.0
313.15	0.0000	0.2278	1012.0
313.15	0.0000	0.4076	1016.0
313.15	0.0000	0.7264	1008.0
313.15	0.0000	1.0000	1000.0
313.15	0.0068	0.0682	1013.0
313.15	0.0111	0.1152	1021.0
313.15	0.0135	0.0677	1026.0
313.15	0.0162	0.1759	1030.0
313.15	0.0202	0.0673	1041.0
313.15	0.0220	0.1139	1041.0
313.15	0.0267	0.0668	1058.0
313.15	0.0318	0.1728	1055.0
313.15	0.0326	0.1126	1063.0
313.15	0.0332	0.0664	1074.0
313.15	0.0430	0.1114	1088.0
313.15	0.0470	0.1699	1085.0
313.15	0.0531	0.1101	1114.0
313.15	0.0617	0.1671	1121.0
323.15	0.0000	0.0687	994.0
323.15	0.0000	0.1122	998.0
323.15	0.0000	0.1643	1002.0
323.15	0.0000	0.2278	1005.0
323.15	0.0000	0.4076	1008.0
323.15	0.0000	0.7264	1001.0
323.15	0.0000	1.0000	992.0
323.15	0.0068	0.0682	1008.0
323.15	0.0111	0.1152	1016.0
323.15	0.0135	0.0677	1022.0
323.15	0.0162	0.1759	1024.0
323.15	0.0202	0.0673	1036.0
323.15	0.0220	0.1139	1036.0
323.15	0.0267	0.0668	1053.0
323.15	0.0318	0.1728	1049.0
323.15	0.0326	0.1126	1058.0
323.15	0.0332	0.0664	1068.0
323.15	0.0430	0.1114	1083.0
323.15	0.0470	0.1699	1080.0
323.15	0.0531	0.1101	1108.0
323.15	0.0617	0.1671	1115.0
343.15	0.0000	0.0687	983.0
343.15	0.0000	0.1122	986.0
343.15	0.0000	0.1643	989.0
343.15	0.0000	0.2278	992.0
343.15	0.0000	0.4076	993.0
343.15	0.0000	0.7264	985.0
343.15	0.0000	1.0000	976.0
343.15	0.0068	0.0682	997.0
343.15	0.0111	0.1152	1004.0
343.15	0.0135	0.0677	1011.0
343.15	0.0162	0.1759	1012.0
343.15	0.0202	0.0673	1025.0
343.15	0.0220	0.1139	1024.0
343.15	0.0267	0.0668	1042.0
343.15	0.0318	0.1728	1037.0
343.15	0.0326	0.1126	1046.0
343.15	0.0332	0.0664	1057.0
343.15	0.0430	0.1114	1072.0
343.15	0.0470	0.1699	1068.0
343.15	0.0617	0.1671	1104.0
353.15	0.0000	0.0687	977.0
353.15	0.0000	0.1122	979.0
353.15	0.0000	0.1643	982.0
353.15	0.0000	0.2278	984.0
353.15	0.0000	0.4076	985.0
353.15	0.0000	0.7264	976.0
353.15	0.0000	1.0000	968.0
353.15	0.0068	0.0682	990.0
353.15	0.0111	0.1152	997.0
353.15	0.0135	0.0677	1004.0
353.15	0.0162	0.1759	1005.0
353.15	0.0202	0.0673	1019.0
353.15	0.0220	0.1139	1018.0
353.15	0.0267	0.0668	1036.0
353.15	0.0318	0.1728	1031.0
353.15	0.0326	0.1126	1040.0
353.15	0.0430	0.1114	1066.0
353.15	0.0470	0.1699	1062.0
353.15	0.0617	0.1671	1098.0

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Solvent: Mass fraction = 0.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Carbon dioxide (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	1010.44
298.15	0.6900	1041.76
298.15	1.23	1066.68
298.15	1.87	1093.32
298.15	2.41	1117.07
299.15	0.0000	1010.01
299.15	0.6900	1041.33
299.15	1.23	1066.14
299.15	1.87	1092.89
299.15	2.41	1116.59
301.15	0.0000	1009.11
301.15	0.6900	1040.44
301.15	1.23	1065.14
301.15	1.87	1091.99
301.15	2.41	1115.64
303.15	0.0000	1008.2
303.15	0.6900	1039.54
303.15	1.23	1064.06
303.15	1.87	1091.07
303.15	2.41	1114.68
313.15	0.0000	1003.32
313.15	0.6900	1034.74
313.15	1.23	1058.86
313.15	1.87	1086.19
313.15	2.41	1109.69
323.15	0.0000	997.9
323.15	0.6900	1029.53
323.15	1.23	1053.28
323.15	1.87	1081.03
323.15	2.41	1104.41
333.15	0.0000	992.21
333.15	0.6900	1023.93
333.15	1.23	1047.69
333.15	1.87	1075.51
343.15	0.0000	985.83
343.15	0.6900	1017.95
343.15	1.23	1041.82
343.15	1.87	1069.66
353.15	0.0000	979.22
353.15	0.6900	1011.44
353.15	1.23	1035.47
353.15	1.87	1063.49

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Fixed		Measured
Amount ratio of solute to solvent of Carbon dioxide (2) - Liquid	Mass ratio of solute to solvent of Water (3) - Liquid	Mass density, kg/m3 - Liquid
0.0000	4.0	1007.1
0.1500	4.0	1029.0
0.2500	4.0	1045.9
0.3500	4.0	1059.0
0.5000	4.0	1081.0
0.0000	2.333	1012.9
0.1500	2.333	1044.2
0.2500	2.333	1065.0
0.3500	2.333	1085.1
0.5000	2.333	1105.0
0.0000	1.5	1018.3
0.1500	1.5	1058.9
0.2500	1.5	1086.6
0.3500	1.5	1112.3
0.5000	1.5	1138.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0091	0.1112	1037.6
298.15	0.0111	0.1110	1033.3
298.15	0.0113	0.1109	1054.4
298.15	0.0135	0.1107	1065.3
298.15	0.0188	0.1101	1062.7
298.15	0.0230	0.1096	1053.4
298.15	0.0245	0.1095	1090.5
298.15	0.0293	0.1089	1094.5
298.15	0.0347	0.1083	1075.6
298.15	0.0374	0.1080	1130.8
298.15	0.0395	0.1078	1129.6
298.15	0.0445	0.1072	1153.6
298.15	0.0471	0.1069	1096.4
298.15	0.0510	0.1065	1166.8
298.15	0.0591	0.1056	1114.2
298.15	0.0617	0.1053	1200.2
298.15	0.0293	0.1089	1099.3
313.15	0.0091	0.1112	1029.5
313.15	0.0111	0.1110	1025.3
313.15	0.0113	0.1109	1044.8
313.15	0.0135	0.1107	1055.4
313.15	0.0188	0.1101	1054.7
313.15	0.0230	0.1096	1046.4
313.15	0.0245	0.1095	1081.7
313.15	0.0293	0.1089	1086.7
313.15	0.0347	0.1083	1066.9
313.15	0.0374	0.1080	1122.5
313.15	0.0395	0.1078	1119.9
313.15	0.0445	0.1072	1145.0
313.15	0.0471	0.1069	1089.1
313.15	0.0510	0.1065	1158.5
313.15	0.0591	0.1056	1106.8
313.15	0.0617	0.1053	1191.6
313.15	0.0293	0.1089	1088.9
323.15	0.0091	0.1112	1023.7
323.15	0.0111	0.1110	1019.6
323.15	0.0113	0.1109	1038.4
323.15	0.0135	0.1107	1048.9
323.15	0.0188	0.1101	1049.0
323.15	0.0230	0.1096	1041.2
323.15	0.0245	0.1095	1075.7
323.15	0.0293	0.1089	1081.1
323.15	0.0347	0.1083	1061.3
323.15	0.0374	0.1080	1116.8
323.15	0.0395	0.1078	1113.8
323.15	0.0445	0.1072	1139.1
323.15	0.0471	0.1069	1083.8
323.15	0.0510	0.1065	1152.8
323.15	0.0591	0.1056	1101.4
323.15	0.0617	0.1053	1185.8
323.15	0.0293	0.1089	1081.7
333.15	0.0091	0.1112	1017.8
333.15	0.0111	0.1110	1013.8
333.15	0.0113	0.1109	1032.0
333.15	0.0135	0.1107	1042.1
333.15	0.0188	0.1101	1043.0
333.15	0.0230	0.1096	1035.6
333.15	0.0245	0.1095	1069.7
333.15	0.0293	0.1089	1074.4
333.15	0.0347	0.1083	1055.6
333.15	0.0374	0.1080	1110.8
333.15	0.0395	0.1078	1108.7
333.15	0.0445	0.1072	1133.1
333.15	0.0471	0.1069	1078.2
333.15	0.0510	0.1065	1146.9
333.15	0.0591	0.1056	1095.7
333.15	0.0617	0.1053	1179.8
333.15	0.0293	0.1089	1075.2
343.15	0.0091	0.1112	1011.0
343.15	0.0111	0.1110	1007.6
343.15	0.0113	0.1109	1025.2
343.15	0.0135	0.1107	1035.1
343.15	0.0188	0.1101	1036.7
343.15	0.0230	0.1096	1029.7
343.15	0.0245	0.1095	1063.2
343.15	0.0293	0.1089	1066.6
343.15	0.0347	0.1083	1049.6
343.15	0.0374	0.1080	1104.8
343.15	0.0395	0.1078	1103.2
343.15	0.0445	0.1072	1127.0
343.15	0.0471	0.1069	1072.3
343.15	0.0510	0.1065	1140.8
343.15	0.0591	0.1056	1088.7
343.15	0.0617	0.1053	1173.7
343.15	0.0293	0.1089	1068.6
353.15	0.0091	0.1112	1004.8
353.15	0.0111	0.1110	1000.2
353.15	0.0113	0.1109	1018.3
353.15	0.0135	0.1107	1028.0
353.15	0.0188	0.1101	1029.2
353.15	0.0230	0.1096	1023.4
353.15	0.0245	0.1095	1056.7
353.15	0.0293	0.1089	1062.6
353.15	0.0347	0.1083	1043.4
353.15	0.0374	0.1080	1098.5
353.15	0.0395	0.1078	1096.3
353.15	0.0445	0.1072	1120.7
353.15	0.0471	0.1069	1066.0
353.15	0.0510	0.1065	1134.5
353.15	0.0591	0.1056	1081.2
353.15	0.0617	0.1053	1167.8
353.15	0.0293	0.1089	1058.0
363.15	0.0091	0.1112	997.0
363.15	0.0111	0.1110	993.6
363.15	0.0113	0.1109	1011.0
363.15	0.0135	0.1107	1020.6
363.15	0.0188	0.1101	1023.2
363.15	0.0230	0.1096	1016.7
363.15	0.0245	0.1095	1049.9
363.15	0.0293	0.1089	1049.4
363.15	0.0347	0.1083	1036.7
363.15	0.0374	0.1080	1092.0
363.15	0.0395	0.1078	1088.8
363.15	0.0445	0.1072	1114.3
363.15	0.0471	0.1069	1059.5
363.15	0.0510	0.1065	1127.3
363.15	0.0591	0.1056	1074.9
363.15	0.0617	0.1053	1160.6
363.15	0.0293	0.1089	1055.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 700 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mass density, kg/m3 - Liquid
373.10	0.0091	0.1112	990.5
373.10	0.0111	0.1110	986.5
373.10	0.0113	0.1109	1004.5
373.10	0.0135	0.1107	1014.5
373.10	0.0188	0.1101	1016.2
373.10	0.0230	0.1096	1009.2
373.10	0.0245	0.1095	1043.0
373.10	0.0293	0.1089	1049.4
373.10	0.0347	0.1083	1030.6
373.10	0.0374	0.1080	1085.4
373.10	0.0395	0.1078	1082.4
373.10	0.0445	0.1072	1107.0
373.10	0.0471	0.1069	1054.5
373.10	0.0510	0.1065	1119.6
373.10	0.0591	0.1056	1069.1
373.10	0.0617	0.1053	1153.7
373.10	0.0293	0.1089	1042.3
383.15	0.0091	0.1112	983.1
383.15	0.0111	0.1110	980.1
383.15	0.0113	0.1109	997.5
383.15	0.0135	0.1107	1007.3
383.15	0.0188	0.1101	1009.2
383.15	0.0230	0.1096	1002.3
383.15	0.0245	0.1095	1036.9
383.15	0.0293	0.1089	1043.9
383.15	0.0347	0.1083	1024.2
383.15	0.0374	0.1080	1079.7
383.15	0.0395	0.1078	1076.6
383.15	0.0445	0.1072	1098.3
383.15	0.0471	0.1069	1048.2
383.15	0.0510	0.1065	1112.5
383.15	0.0591	0.1056	1063.3
383.15	0.0617	0.1053	1147.8
383.15	0.0293	0.1089	1035.3
393.15	0.0091	0.1112	975.7
393.15	0.0111	0.1110	973.7
393.15	0.0113	0.1109	990.8
393.15	0.0135	0.1107	1000.7
393.15	0.0188	0.1101	1002.3
393.15	0.0230	0.1096	995.7
393.15	0.0245	0.1095	1028.8
393.15	0.0293	0.1089	1036.7
393.15	0.0347	0.1083	1018.3
393.15	0.0374	0.1080	1073.9
393.15	0.0395	0.1078	1069.9
393.15	0.0445	0.1072	1092.2
393.15	0.0471	0.1069	1041.7
393.15	0.0510	0.1065	1104.8
393.15	0.0591	0.1056	1057.6
393.15	0.0617	0.1053	1141.3
393.15	0.0293	0.1089	1028.9
403.15	0.0091	0.1112	967.8
403.15	0.0111	0.1110	967.4
403.15	0.0113	0.1109	983.3
403.15	0.0135	0.1107	994.9
403.15	0.0188	0.1101	994.6
403.15	0.0230	0.1096	988.9
403.15	0.0245	0.1095	1021.0
403.15	0.0293	0.1089	1029.8
403.15	0.0347	0.1083	1012.9
403.15	0.0374	0.1080	1067.9
403.15	0.0395	0.1078	1063.1
403.15	0.0445	0.1072	1085.7
403.15	0.0471	0.1069	1036.1
403.15	0.0510	0.1065	1098.4
403.15	0.0591	0.1056	1051.9
403.15	0.0617	0.1053	1136.3
403.15	0.0293	0.1089	1022.3
413.15	0.0091	0.1112	960.5
413.15	0.0111	0.1110	960.5
413.15	0.0113	0.1109	976.8
413.15	0.0135	0.1107	989.6
413.15	0.0188	0.1101	987.6
413.15	0.0230	0.1096	982.6
413.15	0.0245	0.1095	1012.8
413.15	0.0293	0.1089	1023.3
413.15	0.0347	0.1083	1007.9
413.15	0.0374	0.1080	1061.2
413.15	0.0395	0.1078	1057.5
413.15	0.0445	0.1072	1079.5
413.15	0.0471	0.1069	1029.5
413.15	0.0510	0.1065	1092.6
413.15	0.0591	0.1056	1045.6
413.15	0.0617	0.1053	1130.4
413.15	0.0293	0.1089	1017.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mass density, kg/m3 - Liquid
313.15	0.4241	0.2163	1240.9
313.15	0.4278	0.2096	1232.1
313.15	0.4296	0.2062	1232.5
313.15	0.4314	0.2028	1223.4
313.15	0.4333	0.1993	1220.8
313.15	0.4371	0.1923	1216.4
313.15	0.4410	0.1852	1209.0
313.15	0.4449	0.1780	1197.2
313.15	0.4489	0.1706	1189.9
313.15	0.4509	0.1668	1181.5
313.15	0.4550	0.1593	1173.3
313.15	0.4634	0.1437	1158.2
313.15	0.4656	0.1397	1154.0
313.15	0.4678	0.1357	1154.0
313.15	0.4700	0.1316	1148.6
313.15	0.4860	0.1021	1115.0
313.15	0.5214	0.0365	1053.4
313.15	0.4489	0.1706	1188.7
313.15	0.4656	0.1397	1152.0
313.15	0.4860	0.1021	1114.8
313.15	0.4860	0.1021	1117.6
323.15	0.4259	0.2130	1232.3
323.15	0.4278	0.2096	1226.6
323.15	0.4296	0.2062	1226.1
323.15	0.4314	0.2028	1217.1
323.15	0.4333	0.1993	1213.8
323.15	0.4371	0.1923	1210.8
323.15	0.4410	0.1852	1203.7
323.15	0.4449	0.1780	1191.8
323.15	0.4489	0.1706	1184.5
323.15	0.4509	0.1668	1176.0
323.15	0.4550	0.1593	1167.8
323.15	0.4634	0.1437	1150.9
323.15	0.4656	0.1397	1148.2
323.15	0.4678	0.1357	1148.2
323.15	0.4700	0.1316	1142.9
323.15	0.4836	0.1064	1111.1
323.15	0.4860	0.1021	1108.5
323.15	0.5214	0.0365	1046.3
323.15	0.4489	0.1706	1183.0
323.15	0.4656	0.1397	1146.5
323.15	0.4860	0.1021	1108.7
333.15	0.4259	0.2130	1223.9
333.15	0.4278	0.2096	1220.9
333.15	0.4352	0.1958	1207.8
333.15	0.4390	0.1888	1205.2
333.15	0.4410	0.1852	1198.2
333.15	0.4449	0.1780	1185.5
333.15	0.4489	0.1706	1177.3
333.15	0.4509	0.1668	1168.8
333.15	0.4550	0.1593	1161.8
333.15	0.4634	0.1437	1143.6
333.15	0.4656	0.1397	1140.2
333.15	0.4678	0.1357	1135.8
333.15	0.4836	0.1064	1104.5
333.15	0.4860	0.1021	1102.6
333.15	0.5214	0.0365	1039.1
333.15	0.4509	0.1668	1179.3
333.15	0.4678	0.1357	1139.7
333.15	0.4860	0.1021	1101.4
343.15	0.4278	0.2096	1215.1
343.15	0.4352	0.1958	1198.8
343.15	0.4390	0.1888	1198.8
343.15	0.4410	0.1852	1192.3
343.15	0.4449	0.1780	1179.9
343.15	0.4489	0.1706	1174.0
343.15	0.4509	0.1668	1163.6
343.15	0.4550	0.1593	1156.6
343.15	0.4634	0.1437	1138.5
343.15	0.4656	0.1397	1135.0
343.15	0.4678	0.1357	1130.4
343.15	0.4836	0.1064	1098.8
343.15	0.4860	0.1021	1096.7
343.15	0.5214	0.0365	1031.8
343.15	0.4489	0.1706	1171.5
343.15	0.4656	0.1397	1134.5
343.15	0.4860	0.1021	1095.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 800 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0687	0.0000	1003.6
303.15	0.0682	0.0068	1019.1
303.15	0.0677	0.0135	1032.4
303.15	0.0673	0.0202	1046.7
303.15	0.0668	0.0267	1061.1
303.15	0.0664	0.0332	1074.4
313.15	0.0687	0.0000	999.4
313.15	0.0682	0.0068	1014.8
313.15	0.0677	0.0135	1028.1
313.15	0.0673	0.0202	1042.4
313.15	0.0668	0.0267	1056.7
313.15	0.0664	0.0332	1069.8
323.15	0.0687	0.0000	994.6
323.15	0.0682	0.0068	1010.2
323.15	0.0677	0.0135	1023.3
323.15	0.0673	0.0202	1037.6
323.15	0.0668	0.0267	1051.8
323.15	0.0664	0.0332	1064.9
333.15	0.0687	0.0000	989.1
333.15	0.0682	0.0068	1004.8
333.15	0.0677	0.0135	1018.0
333.15	0.0673	0.0202	1032.3
333.15	0.0668	0.0267	1046.4
333.15	0.0664	0.0332	1059.4
303.15	0.1122	0.0000	1008.2
303.15	0.1110	0.0111	1027.8
303.15	0.1097	0.0219	1047.5
303.15	0.1085	0.0326	1066.1
303.15	0.1074	0.0430	1086.3
303.15	0.1062	0.0531	1106.0
313.15	0.1122	0.0000	1003.3
313.15	0.1110	0.0111	1022.9
313.15	0.1097	0.0219	1042.7
313.15	0.1085	0.0326	1061.4
313.15	0.1074	0.0430	1081.5
313.15	0.1062	0.0531	1101.0
323.15	0.1122	0.0000	998.1
323.15	0.1110	0.0111	1017.8
323.15	0.1097	0.0219	1037.6
323.15	0.1085	0.0326	1056.3
323.15	0.1074	0.0430	1076.3
323.15	0.1062	0.0531	1095.8
333.15	0.1122	0.0000	992.3
333.15	0.1110	0.0111	1012.0
333.15	0.1097	0.0219	1032.0
333.15	0.1085	0.0326	1050.7
333.15	0.1074	0.0430	1070.7
333.15	0.1062	0.0531	1090.1
303.15	0.1643	0.0000	1013.3
303.15	0.1616	0.0162	1037.8
303.15	0.1591	0.0318	1062.8
303.15	0.1566	0.0470	1087.6
303.15	0.1542	0.0617	1113.9
303.15	0.1518	0.0759	1139.6
313.15	0.1643	0.0000	1007.8
313.15	0.1616	0.0162	1032.5
313.15	0.1591	0.0318	1057.6
313.15	0.1566	0.0470	1082.5
313.15	0.1542	0.0617	1108.6
313.15	0.1518	0.0759	1134.4
323.15	0.1643	0.0000	1002.1
323.15	0.1616	0.0162	1026.9
323.15	0.1591	0.0318	1052.1
323.15	0.1566	0.0470	1077.1
323.15	0.1542	0.0617	1103.2
323.15	0.1518	0.0759	1129.0
333.15	0.1643	0.0000	995.7
333.15	0.1616	0.0162	1020.8
333.15	0.1591	0.0318	1046.2
333.15	0.1566	0.0470	1071.3
333.15	0.1542	0.0617	1097.5
333.15	0.1518	0.0759	1123.2
303.15	0.2277	0.0000	1017.8
303.15	0.2227	0.0223	1047.2
303.15	0.2178	0.0436	1075.1
303.15	0.2132	0.0640	1106.7
303.15	0.2087	0.0835	1136.4
303.15	0.2045	0.1022	1167.7
313.15	0.2277	0.0000	1011.8
313.15	0.2227	0.0223	1040.6
313.15	0.2178	0.0436	1069.4
313.15	0.2132	0.0640	1099.9
313.15	0.2087	0.0835	1131.0
313.15	0.2045	0.1022	1162.1
323.15	0.2277	0.0000	1005.4
323.15	0.2227	0.0223	1034.4
323.15	0.2178	0.0436	1063.6
323.15	0.2132	0.0640	1093.9
323.15	0.2087	0.0835	1125.4
323.15	0.2045	0.1022	1156.5
333.15	0.2277	0.0000	998.7
333.15	0.2227	0.0223	1027.9
333.15	0.2178	0.0436	1057.4
333.15	0.2132	0.0640	1088.0
333.15	0.2087	0.0835	1119.6
333.15	0.2045	0.1022	1150.7
303.15	0.3067	0.0000	1021.3
303.15	0.2976	0.0298	1058.6
303.15	0.2890	0.0578	1091.6
303.15	0.2808	0.0843	1126.2
303.15	0.2732	0.1093	1162.1
303.15	0.2659	0.1330	1197.6
313.15	0.3067	0.0000	1014.6
313.15	0.2976	0.0298	1052.3
313.15	0.2890	0.0578	1085.6
313.15	0.2808	0.0843	1120.4
313.15	0.2732	0.1093	1156.5
313.15	0.2659	0.1330	1192.0
323.15	0.3067	0.0000	1007.8
323.15	0.2976	0.0298	1045.9
323.15	0.2890	0.0578	1079.5
323.15	0.2808	0.0843	1114.6
323.15	0.2732	0.1093	1150.8
323.15	0.2659	0.1330	1186.3
333.15	0.3067	0.0000	1000.6
333.15	0.2976	0.0298	1039.2
333.15	0.2890	0.0578	1073.1
333.15	0.2808	0.0843	1108.5
333.15	0.2732	0.1093	1144.9
333.15	0.2659	0.1330	1180.4
303.15	0.4076	0.0000	1022.6
303.15	0.3916	0.0392	1063.9
303.15	0.3769	0.0754	1101.1
303.15	0.3632	0.1090	1143.7
303.15	0.3505	0.1402	1185.4
303.15	0.3386	0.1693	1226.2
313.15	0.4076	0.0000	1015.5
313.15	0.3916	0.0392	1057.3
313.15	0.3769	0.0754	1094.8
313.15	0.3632	0.1090	1137.8
313.15	0.3505	0.1402	1179.7
313.15	0.3386	0.1693	1220.4
323.15	0.4076	0.0000	1008.2
323.15	0.3916	0.0392	1050.6
323.15	0.3769	0.0754	1088.4
323.15	0.3632	0.1090	1131.8
323.15	0.3505	0.1402	1174.0
323.15	0.3386	0.1693	1214.7
333.15	0.4076	0.0000	1000.6
333.15	0.3916	0.0392	1043.6
333.15	0.3769	0.0754	1081.9
333.15	0.3632	0.1090	1125.6
333.15	0.3505	0.1402	1168.1
333.15	0.3386	0.1693	1208.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Solvent: Mass fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0620	0.0000	293.15	1000.88
0.0620	0.0000	303.15	998.06
0.0620	0.0000	313.15	994.42
0.0620	0.0000	323.15	990.09
0.0620	0.0000	333.15	985.12
0.0620	0.0000	343.15	978.86
0.0620	0.0000	353.15	973.57
0.0620	0.0019	293.15	1004.95
0.0620	0.0019	303.15	1002.16
0.0620	0.0019	313.15	998.47
0.0620	0.0019	323.15	994.07
0.0620	0.0019	333.15	989.1
0.0620	0.0019	343.15	983.58
0.0620	0.0019	353.15	977.56
0.0620	0.0037	293.15	1009.77
0.0620	0.0037	303.15	1006.8
0.0620	0.0037	313.15	1003.09
0.0620	0.0037	323.15	998.72
0.0620	0.0037	333.15	993.75
0.0620	0.0037	343.15	988.22
0.0620	0.0037	353.15	981.76
0.0620	0.0068	293.15	1017.47
0.0620	0.0068	303.15	1014.52
0.0620	0.0068	313.15	1010.79
0.0620	0.0068	323.15	1006.21
0.0620	0.0068	333.15	1001.33
0.0620	0.0068	343.15	995.87
0.0620	0.0068	353.15	989.89
0.0620	0.0089	293.15	1022.17
0.0620	0.0089	303.15	1019.0
0.0620	0.0089	313.15	1015.13
0.0620	0.0089	323.15	1010.67
0.0620	0.0089	333.15	1005.6
0.0620	0.0089	343.15	1000.03
0.0620	0.0089	353.15	993.98
0.3000	0.0000	293.15	1012.68
0.3000	0.0000	298.15	1010.55
0.3000	0.0000	303.15	1008.31
0.3000	0.0000	313.15	1003.45
0.3000	0.0000	323.15	998.07
0.3000	0.0000	333.15	992.23
0.3000	0.0000	343.15	985.96
0.3000	0.0000	353.15	979.27
0.3000	0.0130	293.15	1030.99
0.3000	0.0130	298.15	1028.87
0.3000	0.0130	303.15	1026.65
0.3000	0.0130	313.15	1021.88
0.3000	0.0130	323.15	1016.6
0.3000	0.0130	333.15	1010.9
0.3000	0.0130	343.15	1004.8
0.3000	0.0130	353.15	998.31
0.3000	0.0215	293.15	1046.92
0.3000	0.0215	298.15	1044.8
0.3000	0.0215	303.15	1042.58
0.3000	0.0215	313.15	1037.84
0.3000	0.0215	323.15	1032.62
0.3000	0.0215	333.15	1027.0
0.3000	0.0215	343.15	1021.01
0.3000	0.0215	353.15	1014.66
0.3000	0.0328	293.15	1068.9
0.3000	0.0328	298.15	1066.76
0.3000	0.0328	303.15	1064.53
0.3000	0.0328	313.15	1059.81
0.3000	0.0328	323.15	1054.64
0.3000	0.0328	333.15	1049.12
0.3000	0.0328	343.15	1043.23
0.3000	0.0328	353.15	1037.04
0.3000	0.0431	293.15	1086.89
0.3000	0.0431	298.15	1084.7
0.3000	0.0431	303.15	1082.44
0.3000	0.0431	313.15	1077.75
0.3000	0.0431	323.15	1072.6
0.3000	0.0431	333.15	1067.11
0.3000	0.0431	343.15	1061.28
0.3000	0.0431	353.15	1055.16
0.3000	0.0544	293.15	1108.2
0.3000	0.0544	298.15	1105.88
0.3000	0.0544	303.15	1103.51
0.3000	0.0544	313.15	1098.66
0.3000	0.0544	323.15	1093.45
0.3000	0.0544	333.15	1087.88
0.3000	0.0544	343.15	1082.0
0.3000	0.0544	353.15	1075.85

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	0.0687	1005.0
298.15	0.0000	0.1122	1011.0
298.15	0.0000	0.1643	1016.0
298.15	0.0000	0.2278	1021.0
298.15	0.0000	0.4076	1026.0
298.15	0.0000	0.7264	1020.0
298.15	0.0000	1.0000	1012.0
298.15	0.0068	0.0682	1019.0
298.15	0.0111	0.1152	1028.0
298.15	0.0135	0.0677	1033.0
298.15	0.0162	0.1759	1038.0
298.15	0.0202	0.0673	1048.0
298.15	0.0220	0.1139	1048.0
298.15	0.0267	0.0668	1064.0
298.15	0.0318	0.1728	1063.0
298.15	0.0326	0.1126	1070.0
298.15	0.0332	0.0664	1080.0
298.15	0.0430	0.1114	1096.0
298.15	0.0470	0.1699	1093.0
298.15	0.0531	0.1101	1121.0
298.15	0.0617	0.1671	1129.0
298.15	0.0759	0.1643	1160.0
313.15	0.0000	0.0687	999.0
313.15	0.0000	0.1122	1003.0
313.15	0.0000	0.1643	1008.0
313.15	0.0000	0.2278	1012.0
313.15	0.0000	0.4076	1016.0
313.15	0.0000	0.7264	1008.0
313.15	0.0000	1.0000	1000.0
313.15	0.0068	0.0682	1013.0
313.15	0.0111	0.1152	1021.0
313.15	0.0135	0.0677	1026.0
313.15	0.0162	0.1759	1030.0
313.15	0.0202	0.0673	1041.0
313.15	0.0220	0.1139	1041.0
313.15	0.0267	0.0668	1058.0
313.15	0.0318	0.1728	1055.0
313.15	0.0326	0.1126	1063.0
313.15	0.0332	0.0664	1074.0
313.15	0.0430	0.1114	1088.0
313.15	0.0470	0.1699	1085.0
313.15	0.0531	0.1101	1114.0
313.15	0.0617	0.1671	1121.0
323.15	0.0000	0.0687	994.0
323.15	0.0000	0.1122	998.0
323.15	0.0000	0.1643	1002.0
323.15	0.0000	0.2278	1005.0
323.15	0.0000	0.4076	1008.0
323.15	0.0000	0.7264	1001.0
323.15	0.0000	1.0000	992.0
323.15	0.0068	0.0682	1008.0
323.15	0.0111	0.1152	1016.0
323.15	0.0135	0.0677	1022.0
323.15	0.0162	0.1759	1024.0
323.15	0.0202	0.0673	1036.0
323.15	0.0220	0.1139	1036.0
323.15	0.0267	0.0668	1053.0
323.15	0.0318	0.1728	1049.0
323.15	0.0326	0.1126	1058.0
323.15	0.0332	0.0664	1068.0
323.15	0.0430	0.1114	1083.0
323.15	0.0470	0.1699	1080.0
323.15	0.0531	0.1101	1108.0
323.15	0.0617	0.1671	1115.0
343.15	0.0000	0.0687	983.0
343.15	0.0000	0.1122	986.0
343.15	0.0000	0.1643	989.0
343.15	0.0000	0.2278	992.0
343.15	0.0000	0.4076	993.0
343.15	0.0000	0.7264	985.0
343.15	0.0000	1.0000	976.0
343.15	0.0068	0.0682	997.0
343.15	0.0111	0.1152	1004.0
343.15	0.0135	0.0677	1011.0
343.15	0.0162	0.1759	1012.0
343.15	0.0202	0.0673	1025.0
343.15	0.0220	0.1139	1024.0
343.15	0.0267	0.0668	1042.0
343.15	0.0318	0.1728	1037.0
343.15	0.0326	0.1126	1046.0
343.15	0.0332	0.0664	1057.0
343.15	0.0430	0.1114	1072.0
343.15	0.0470	0.1699	1068.0
343.15	0.0617	0.1671	1104.0
353.15	0.0000	0.0687	977.0
353.15	0.0000	0.1122	979.0
353.15	0.0000	0.1643	982.0
353.15	0.0000	0.2278	984.0
353.15	0.0000	0.4076	985.0
353.15	0.0000	0.7264	976.0
353.15	0.0000	1.0000	968.0
353.15	0.0068	0.0682	990.0
353.15	0.0111	0.1152	997.0
353.15	0.0135	0.0677	1004.0
353.15	0.0162	0.1759	1005.0
353.15	0.0202	0.0673	1019.0
353.15	0.0220	0.1139	1018.0
353.15	0.0267	0.0668	1036.0
353.15	0.0318	0.1728	1031.0
353.15	0.0326	0.1126	1040.0
353.15	0.0430	0.1114	1066.0
353.15	0.0470	0.1699	1062.0
353.15	0.0617	0.1671	1098.0

Surface tension liquid-gas, N/m [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
313.15	0.4259	0.2130	0.0664
313.15	0.4489	0.1706	0.0617
313.15	0.4656	0.1397	0.0594
313.15	0.4836	0.1064	0.0571
313.15	0.5214	0.0365	0.0530
313.15	0.5412	0.0000	0.0515
323.15	0.4259	0.2130	0.0647
323.15	0.4489	0.1706	0.0605
323.15	0.4656	0.1397	0.0589
323.15	0.4836	0.1064	0.0561
323.15	0.5214	0.0365	0.0517
323.15	0.5412	0.0000	0.0504
333.15	0.4259	0.2130	0.0639
333.15	0.4489	0.1706	0.0597
333.15	0.4656	0.1397	0.0570
333.15	0.4836	0.1064	0.0546
333.15	0.5214	0.0365	0.0506
333.15	0.5412	0.0000	0.0493
343.15	0.4259	0.2130	0.0628
343.15	0.4489	0.1706	0.0584
343.15	0.4656	0.1397	0.0562
343.15	0.4836	0.1064	0.0541
343.15	0.5214	0.0365	0.0497
343.15	0.5412	0.0000	0.0481

Surface tension liquid-gas, N/m [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
303.15	0.0687	0.0000	0.0667
303.15	0.0682	0.0068	0.0676
303.15	0.0677	0.0135	0.0684
303.15	0.0673	0.0202	0.0697
303.15	0.0668	0.0267	0.0714
303.15	0.0664	0.0332	0.0736
313.15	0.0687	0.0000	0.0652
313.15	0.0682	0.0068	0.0663
313.15	0.0677	0.0135	0.0670
313.15	0.0673	0.0202	0.0679
313.15	0.0668	0.0267	0.0700
313.15	0.0664	0.0332	0.0718
323.15	0.0687	0.0000	0.0636
323.15	0.0682	0.0068	0.0647
323.15	0.0677	0.0135	0.0654
323.15	0.0673	0.0202	0.0664
323.15	0.0668	0.0267	0.0684
323.15	0.0664	0.0332	0.0702
333.15	0.0687	0.0000	0.0616
333.15	0.0682	0.0068	0.0631
333.15	0.0677	0.0135	0.0638
333.15	0.0673	0.0202	0.0649
333.15	0.0668	0.0267	0.0664
333.15	0.0664	0.0332	0.0689
303.15	0.1122	0.0000	0.0637
303.15	0.1110	0.0111	0.0650
303.15	0.1097	0.0219	0.0664
303.15	0.1085	0.0326	0.0678
303.15	0.1074	0.0430	0.0698
303.15	0.1062	0.0531	0.0728
313.15	0.1122	0.0000	0.0624
313.15	0.1110	0.0111	0.0636
313.15	0.1097	0.0219	0.0650
313.15	0.1085	0.0326	0.0662
313.15	0.1074	0.0430	0.0683
313.15	0.1062	0.0531	0.0714
323.15	0.1122	0.0000	0.0610
323.15	0.1110	0.0111	0.0620
323.15	0.1097	0.0219	0.0632
323.15	0.1085	0.0326	0.0647
323.15	0.1074	0.0430	0.0669
323.15	0.1062	0.0531	0.0698
333.15	0.1122	0.0000	0.0595
333.15	0.1110	0.0111	0.0605
333.15	0.1097	0.0219	0.0615
333.15	0.1085	0.0326	0.0628
333.15	0.1074	0.0430	0.0652
333.15	0.1062	0.0531	0.0685
303.15	0.1643	0.0000	0.0615
303.15	0.1616	0.0162	0.0630
303.15	0.1591	0.0318	0.0646
303.15	0.1566	0.0470	0.0663
303.15	0.1542	0.0617	0.0693
303.15	0.1518	0.0759	0.0724
313.15	0.1643	0.0000	0.0598
313.15	0.1616	0.0162	0.0619
313.15	0.1591	0.0318	0.0634
313.15	0.1566	0.0470	0.0651
313.15	0.1542	0.0617	0.0681
313.15	0.1518	0.0759	0.0711
323.15	0.1643	0.0000	0.0584
323.15	0.1616	0.0162	0.0603
323.15	0.1591	0.0318	0.0620
323.15	0.1566	0.0470	0.0638
323.15	0.1542	0.0617	0.0667
323.15	0.1518	0.0759	0.0698
333.15	0.1643	0.0000	0.0570
333.15	0.1616	0.0162	0.0587
333.15	0.1591	0.0318	0.0602
333.15	0.1566	0.0470	0.0624
333.15	0.1542	0.0617	0.0649
333.15	0.1518	0.0759	0.0681
303.15	0.2277	0.0000	0.0596
303.15	0.2227	0.0223	0.0609
303.15	0.2178	0.0436	0.0627
303.15	0.2132	0.0640	0.0644
303.15	0.2087	0.0835	0.0671
303.15	0.2045	0.1022	0.0705
313.15	0.2277	0.0000	0.0581
313.15	0.2227	0.0223	0.0594
313.15	0.2178	0.0436	0.0613
313.15	0.2132	0.0640	0.0631
313.15	0.2087	0.0835	0.0660
313.15	0.2045	0.1022	0.0695
323.15	0.2277	0.0000	0.0565
323.15	0.2227	0.0223	0.0582
323.15	0.2178	0.0436	0.0596
323.15	0.2132	0.0640	0.0618
323.15	0.2087	0.0835	0.0648
323.15	0.2045	0.1022	0.0682
333.15	0.2277	0.0000	0.0551
333.15	0.2227	0.0223	0.0567
333.15	0.2178	0.0436	0.0579
333.15	0.2132	0.0640	0.0604
333.15	0.2087	0.0835	0.0634
333.15	0.2045	0.1022	0.0670
303.15	0.3067	0.0000	0.0574
303.15	0.2976	0.0298	0.0589
303.15	0.2890	0.0578	0.0606
303.15	0.2808	0.0843	0.0633
303.15	0.2732	0.1093	0.0663
303.15	0.2659	0.1330	0.0707
313.15	0.3067	0.0000	0.0561
313.15	0.2976	0.0298	0.0576
313.15	0.2890	0.0578	0.0596
313.15	0.2808	0.0843	0.0622
313.15	0.2732	0.1093	0.0655
313.15	0.2659	0.1330	0.0698
323.15	0.3067	0.0000	0.0550
323.15	0.2976	0.0298	0.0564
323.15	0.2890	0.0578	0.0586
323.15	0.2808	0.0843	0.0608
323.15	0.2732	0.1093	0.0643
323.15	0.2659	0.1330	0.0686
333.15	0.3067	0.0000	0.0536
333.15	0.2976	0.0298	0.0549
333.15	0.2890	0.0578	0.0573
333.15	0.2808	0.0843	0.0595
333.15	0.2732	0.1093	0.0631
333.15	0.2659	0.1330	0.0672
303.15	0.4076	0.0000	0.0545
303.15	0.3916	0.0392	0.0570
303.15	0.3769	0.0754	0.0590
303.15	0.3632	0.1090	0.0612
303.15	0.3505	0.1402	0.0655
303.15	0.3386	0.1693	0.0692
313.15	0.4076	0.0000	0.0536
313.15	0.3916	0.0392	0.0559
313.15	0.3769	0.0754	0.0580
313.15	0.3632	0.1090	0.0606
313.15	0.3505	0.1402	0.0648
313.15	0.3386	0.1693	0.0684
323.15	0.4076	0.0000	0.0525
323.15	0.3916	0.0392	0.0545
323.15	0.3769	0.0754	0.0568
323.15	0.3632	0.1090	0.0594
323.15	0.3505	0.1402	0.0638
323.15	0.3386	0.1693	0.0673
333.15	0.4076	0.0000	0.0512
333.15	0.3916	0.0392	0.0530
333.15	0.3769	0.0754	0.0555
333.15	0.3632	0.1090	0.0582
333.15	0.3505	0.1402	0.0627
333.15	0.3386	0.1693	0.0662

Surface tension liquid-gas, N/m [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
313.15	0.4259	0.2130	0.0664
313.15	0.4489	0.1706	0.0617
313.15	0.4656	0.1397	0.0594
313.15	0.4836	0.1064	0.0571
313.15	0.5214	0.0365	0.0530
313.15	0.5412	0.0000	0.0515
323.15	0.4259	0.2130	0.0647
323.15	0.4489	0.1706	0.0605
323.15	0.4656	0.1397	0.0589
323.15	0.4836	0.1064	0.0561
323.15	0.5214	0.0365	0.0517
323.15	0.5412	0.0000	0.0504
333.15	0.4259	0.2130	0.0639
333.15	0.4489	0.1706	0.0597
333.15	0.4656	0.1397	0.0570
333.15	0.4836	0.1064	0.0546
333.15	0.5214	0.0365	0.0506
333.15	0.5412	0.0000	0.0493
343.15	0.4259	0.2130	0.0628
343.15	0.4489	0.1706	0.0584
343.15	0.4656	0.1397	0.0562
343.15	0.4836	0.1064	0.0541
343.15	0.5214	0.0365	0.0497
343.15	0.5412	0.0000	0.0481

Surface tension liquid-gas, N/m [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Monoethanolamine (1) - Liquid	Mole fraction of Carbon dioxide (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
303.15	0.0687	0.0000	0.0667
303.15	0.0682	0.0068	0.0676
303.15	0.0677	0.0135	0.0684
303.15	0.0673	0.0202	0.0697
303.15	0.0668	0.0267	0.0714
303.15	0.0664	0.0332	0.0736
313.15	0.0687	0.0000	0.0652
313.15	0.0682	0.0068	0.0663
313.15	0.0677	0.0135	0.0670
313.15	0.0673	0.0202	0.0679
313.15	0.0668	0.0267	0.0700
313.15	0.0664	0.0332	0.0718
323.15	0.0687	0.0000	0.0636
323.15	0.0682	0.0068	0.0647
323.15	0.0677	0.0135	0.0654
323.15	0.0673	0.0202	0.0664
323.15	0.0668	0.0267	0.0684
323.15	0.0664	0.0332	0.0702
333.15	0.0687	0.0000	0.0616
333.15	0.0682	0.0068	0.0631
333.15	0.0677	0.0135	0.0638
333.15	0.0673	0.0202	0.0649
333.15	0.0668	0.0267	0.0664
333.15	0.0664	0.0332	0.0689
303.15	0.1122	0.0000	0.0637
303.15	0.1110	0.0111	0.0650
303.15	0.1097	0.0219	0.0664
303.15	0.1085	0.0326	0.0678
303.15	0.1074	0.0430	0.0698
303.15	0.1062	0.0531	0.0728
313.15	0.1122	0.0000	0.0624
313.15	0.1110	0.0111	0.0636
313.15	0.1097	0.0219	0.0650
313.15	0.1085	0.0326	0.0662
313.15	0.1074	0.0430	0.0683
313.15	0.1062	0.0531	0.0714
323.15	0.1122	0.0000	0.0610
323.15	0.1110	0.0111	0.0620
323.15	0.1097	0.0219	0.0632
323.15	0.1085	0.0326	0.0647
323.15	0.1074	0.0430	0.0669
323.15	0.1062	0.0531	0.0698
333.15	0.1122	0.0000	0.0595
333.15	0.1110	0.0111	0.0605
333.15	0.1097	0.0219	0.0615
333.15	0.1085	0.0326	0.0628
333.15	0.1074	0.0430	0.0652
333.15	0.1062	0.0531	0.0685
303.15	0.1643	0.0000	0.0615
303.15	0.1616	0.0162	0.0630
303.15	0.1591	0.0318	0.0646
303.15	0.1566	0.0470	0.0663
303.15	0.1542	0.0617	0.0693
303.15	0.1518	0.0759	0.0724
313.15	0.1643	0.0000	0.0598
313.15	0.1616	0.0162	0.0619
313.15	0.1591	0.0318	0.0634
313.15	0.1566	0.0470	0.0651
313.15	0.1542	0.0617	0.0681
313.15	0.1518	0.0759	0.0711
323.15	0.1643	0.0000	0.0584
323.15	0.1616	0.0162	0.0603
323.15	0.1591	0.0318	0.0620
323.15	0.1566	0.0470	0.0638
323.15	0.1542	0.0617	0.0667
323.15	0.1518	0.0759	0.0698
333.15	0.1643	0.0000	0.0570
333.15	0.1616	0.0162	0.0587
333.15	0.1591	0.0318	0.0602
333.15	0.1566	0.0470	0.0624
333.15	0.1542	0.0617	0.0649
333.15	0.1518	0.0759	0.0681
303.15	0.2277	0.0000	0.0596
303.15	0.2227	0.0223	0.0609
303.15	0.2178	0.0436	0.0627
303.15	0.2132	0.0640	0.0644
303.15	0.2087	0.0835	0.0671
303.15	0.2045	0.1022	0.0705
313.15	0.2277	0.0000	0.0581
313.15	0.2227	0.0223	0.0594
313.15	0.2178	0.0436	0.0613
313.15	0.2132	0.0640	0.0631
313.15	0.2087	0.0835	0.0660
313.15	0.2045	0.1022	0.0695
323.15	0.2277	0.0000	0.0565
323.15	0.2227	0.0223	0.0582
323.15	0.2178	0.0436	0.0596
323.15	0.2132	0.0640	0.0618
323.15	0.2087	0.0835	0.0648
323.15	0.2045	0.1022	0.0682
333.15	0.2277	0.0000	0.0551
333.15	0.2227	0.0223	0.0567
333.15	0.2178	0.0436	0.0579
333.15	0.2132	0.0640	0.0604
333.15	0.2087	0.0835	0.0634
333.15	0.2045	0.1022	0.0670
303.15	0.3067	0.0000	0.0574
303.15	0.2976	0.0298	0.0589
303.15	0.2890	0.0578	0.0606
303.15	0.2808	0.0843	0.0633
303.15	0.2732	0.1093	0.0663
303.15	0.2659	0.1330	0.0707
313.15	0.3067	0.0000	0.0561
313.15	0.2976	0.0298	0.0576
313.15	0.2890	0.0578	0.0596
313.15	0.2808	0.0843	0.0622
313.15	0.2732	0.1093	0.0655
313.15	0.2659	0.1330	0.0698
323.15	0.3067	0.0000	0.0550
323.15	0.2976	0.0298	0.0564
323.15	0.2890	0.0578	0.0586
323.15	0.2808	0.0843	0.0608
323.15	0.2732	0.1093	0.0643
323.15	0.2659	0.1330	0.0686
333.15	0.3067	0.0000	0.0536
333.15	0.2976	0.0298	0.0549
333.15	0.2890	0.0578	0.0573
333.15	0.2808	0.0843	0.0595
333.15	0.2732	0.1093	0.0631
333.15	0.2659	0.1330	0.0672
303.15	0.4076	0.0000	0.0545
303.15	0.3916	0.0392	0.0570
303.15	0.3769	0.0754	0.0590
303.15	0.3632	0.1090	0.0612
303.15	0.3505	0.1402	0.0655
303.15	0.3386	0.1693	0.0692
313.15	0.4076	0.0000	0.0536
313.15	0.3916	0.0392	0.0559
313.15	0.3769	0.0754	0.0580
313.15	0.3632	0.1090	0.0606
313.15	0.3505	0.1402	0.0648
313.15	0.3386	0.1693	0.0684
323.15	0.4076	0.0000	0.0525
323.15	0.3916	0.0392	0.0545
323.15	0.3769	0.0754	0.0568
323.15	0.3632	0.1090	0.0594
323.15	0.3505	0.1402	0.0638
323.15	0.3386	0.1693	0.0673
333.15	0.4076	0.0000	0.0512
333.15	0.3916	0.0392	0.0530
333.15	0.3769	0.0754	0.0555
333.15	0.3632	0.1090	0.0582
333.15	0.3505	0.1402	0.0627
333.15	0.3386	0.1693	0.0662

Sources

• High pressure solubility of carbon dioxide (CO2) in aqueous piperazine solutions
• Experiment and model for the viscosity of carbonated MDEA - MEA aqueous solutions
• CO2 solubility measurement and thermodynamic modeling for 1-methylpiperazine/water/CO2
• Vapor-liquid equilibrium measurement and ENRTL Modeling of CO2 absorption in aqueous hexamethylenediamine
• Equilibrium solubility of carbon dioxide in aqueous solutions of (diethylenetriamine + piperazine)
• Carbon dioxide solubility in aqueous potassium salt solutions of L-proline and DL-.alpha.-aminobutyric acid at high pressures
• CO2 solubility in aqueous potassium lysinate solutions at absorber conditions
• Absorption performance of (CO2 + N2) gas mixtures in amino acid ionic liquids promoted N-methyldiethanolamine aqueous solutions
• CO2 absorption using aqueous potassium lysinate solutions: Vapor - liquid equilibrium data and modelling
• Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
• Vapour-liquid equilibrium study of tertiary amines, single and in blend with 3-(methylamino)propylamine, for post-combustion CO2 capture
• Density and Viscosity of Partially Carbonated Aqueous Tertiary Alkanolamine Solutions at Temperatures between (298.15 and 353.15) K
• Characteristics of Potassium Prolinate + Water + Ethanol Solution as a Phase Changing Absorbent for CO2 Capture
• Density, Viscosity, Refractive Index, and Electrical Conductivity of Degraded Monoethanolamine Solutions at Standard Temperatures
• Investigation of Thermodynamic Properties on CO2 Absorbents Blended with Ammonia, Amino Acids, and Corrosion Inhibitors at 313.15, 333.15, and 353.15 K
• Density, Viscosity, and Performances of Carbon Dioxide Capture in 16 Absorbents of Amine + Ionic Liquid + H2O, Ionic Liquid + H2O, and Amine + H2O Systems
• Density, Viscosity, Heat Capacity, Surface Tension, and Solubility of CO2 in Aqueous Solutions of Potassium Serinate
• CO2 Absorption Rate into Concentrated Aqueous Monoethanolamine and Piperazine
• Density of Water (1) + Monoethanolamine (2) + CO2 (3) from (298.15 to 413.15) K and Surface Tension of Water (1) + Monoethanolamine (2) from (303.15 to 333.15) K
• Density and Surface Tension Measurements of Partially Carbonated Aqueous Monoethanolamine Solutions
• Solubility of Carbon Dioxide in Aqueous Solutions of Monoethanolamine in the Low and High Gas Loading Regions
• Densities and Surface Tensions of CO2 Loaded Aqueous Monoethanolamine Solutions with r = (0.2 to 0.7) at T = (303.15 to 333.15) K
• Equilibrium Total Pressure and CO2 Solubility in Binary and Ternary Aqueous Solutions of 2-(Diethylamino)ethanol (DEEA) and 3-(Methylamino)propylamine (MAPA)
• Physical Properties of Partially CO2 Loaded Aqueous Monoethanolamine (MEA)
• Density and Viscosity of Monoethanolamine + Water + Carbon Dioxide from (25 to 80) deg C