Mixture of Carbon dioxide + 1,6-Hexanediamine + Water

Datasets

1. Mole fraction (2)

Mole fraction of Carbon dioxide (1) [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Carbon dioxide (1) - Liquid
303.15	2.04	0.9640	0.0200
303.15	3.77	0.9620	0.0210
303.15	13.14	0.9570	0.0260
303.15	27.39	0.9550	0.0290
303.15	44.43	0.9540	0.0300
303.15	59.66	0.9540	0.0300
303.15	85.19	0.9530	0.0310
303.15	104.67	0.9520	0.0310
313.15	0.96	0.9670	0.0170
313.15	2.36	0.9650	0.0180
313.15	15.16	0.9600	0.0240
313.15	37.08	0.9570	0.0260
313.15	55.64	0.9560	0.0280
313.15	69.54	0.9550	0.0290
313.15	82.05	0.9540	0.0290
313.15	89.26	0.9540	0.0290
313.15	108.18	0.9530	0.0300
323.15	2.55	0.9660	0.0170
323.15	21.28	0.9610	0.0230
323.15	42.81	0.9590	0.0250
323.15	54.56	0.9580	0.0260
323.15	71.87	0.9570	0.0270
323.15	82.51	0.9570	0.0270
323.15	96.92	0.9560	0.0280
323.15	108.94	0.9550	0.0280
333.15	2.13	0.9680	0.0150
333.15	14.84	0.9650	0.0190
333.15	34.32	0.9620	0.0220
333.15	45.05	0.9610	0.0220
333.15	62.43	0.9600	0.0240
333.15	70.18	0.9590	0.0240
333.15	83.34	0.9590	0.0250
333.15	94.73	0.9580	0.0250
333.15	108.01	0.9570	0.0260
303.15	1.44	0.9270	0.0370
303.15	3.10	0.9240	0.0400
303.15	15.50	0.9160	0.0490
303.15	30.66	0.9120	0.0520
303.15	46.70	0.9100	0.0550
303.15	66.12	0.9080	0.0570
303.15	82.50	0.9060	0.0590
303.15	103.23	0.9050	0.0600
313.15	1.95	0.9290	0.0350
313.15	13.87	0.9200	0.0440
313.15	32.05	0.9150	0.0500
313.15	47.80	0.9130	0.0520
313.15	64.45	0.9110	0.0540
313.15	75.39	0.9100	0.0550
313.15	94.44	0.9080	0.0560
313.15	110.27	0.9080	0.0570
323.15	3.41	0.9300	0.0340
323.15	20.58	0.9230	0.0420
323.15	38.28	0.9180	0.0460
323.15	46.68	0.9170	0.0470
323.15	52.53	0.9170	0.0480
323.15	65.17	0.9150	0.0490
323.15	80.30	0.9140	0.0500
323.15	101.83	0.9130	0.0520
333.15	3.17	0.9330	0.0310
333.15	12.84	0.9290	0.0350
333.15	35.87	0.9230	0.0420
333.15	53.14	0.9200	0.0440
333.15	62.24	0.9190	0.0450
333.15	73.55	0.9180	0.0460
333.15	84.64	0.9170	0.0470
333.15	100.39	0.9160	0.0480
303.15	1.41	0.8850	0.0570
303.15	3.93	0.8800	0.0620
303.15	6.96	0.8760	0.0660
303.15	11.84	0.8730	0.0690
303.15	18.65	0.8700	0.0720
303.15	30.05	0.8660	0.0760
303.15	51.18	0.8620	0.0810
303.15	76.44	0.8580	0.0850
303.15	105.81	0.8570	0.0860
313.15	2.35	0.8860	0.0550
313.15	9.31	0.8790	0.0630
313.15	14.44	0.8760	0.0660
313.15	17.66	0.8740	0.0680
313.15	23.24	0.8720	0.0700
313.15	41.52	0.8680	0.0740
313.15	59.20	0.8650	0.0770
313.15	75.39	0.8640	0.0790
313.15	92.08	0.8620	0.0800
323.15	2.22	0.8890	0.0520
323.15	3.50	0.8870	0.0540
323.15	14.27	0.8830	0.0580
323.15	28.99	0.8770	0.0650
323.15	41.77	0.8740	0.0680
323.15	56.94	0.8730	0.0690
323.15	74.16	0.8710	0.0710
323.15	94.98	0.8680	0.0740
333.15	2.48	0.8930	0.0480
333.15	6.27	0.8900	0.0510
333.15	17.52	0.8850	0.0560
333.15	32.37	0.8810	0.0610
333.15	47.11	0.8780	0.0640
333.15	62.72	0.8760	0.0660
333.15	77.52	0.8740	0.0680
333.15	121.88	0.8700	0.0720

Mole fraction of Carbon dioxide (1) [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Carbon dioxide (1) - Liquid
303.15	2.04	0.9640	0.0200
303.15	3.77	0.9620	0.0210
303.15	13.14	0.9570	0.0260
303.15	27.39	0.9550	0.0290
303.15	44.43	0.9540	0.0300
303.15	59.66	0.9540	0.0300
303.15	85.19	0.9530	0.0310
303.15	104.67	0.9520	0.0310
313.15	0.96	0.9670	0.0170
313.15	2.36	0.9650	0.0180
313.15	15.16	0.9600	0.0240
313.15	37.08	0.9570	0.0260
313.15	55.64	0.9560	0.0280
313.15	69.54	0.9550	0.0290
313.15	82.05	0.9540	0.0290
313.15	89.26	0.9540	0.0290
313.15	108.18	0.9530	0.0300
323.15	2.55	0.9660	0.0170
323.15	21.28	0.9610	0.0230
323.15	42.81	0.9590	0.0250
323.15	54.56	0.9580	0.0260
323.15	71.87	0.9570	0.0270
323.15	82.51	0.9570	0.0270
323.15	96.92	0.9560	0.0280
323.15	108.94	0.9550	0.0280
333.15	2.13	0.9680	0.0150
333.15	14.84	0.9650	0.0190
333.15	34.32	0.9620	0.0220
333.15	45.05	0.9610	0.0220
333.15	62.43	0.9600	0.0240
333.15	70.18	0.9590	0.0240
333.15	83.34	0.9590	0.0250
333.15	94.73	0.9580	0.0250
333.15	108.01	0.9570	0.0260
303.15	1.44	0.9270	0.0370
303.15	3.10	0.9240	0.0400
303.15	15.50	0.9160	0.0490
303.15	30.66	0.9120	0.0520
303.15	46.70	0.9100	0.0550
303.15	66.12	0.9080	0.0570
303.15	82.50	0.9060	0.0590
303.15	103.23	0.9050	0.0600
313.15	1.95	0.9290	0.0350
313.15	13.87	0.9200	0.0440
313.15	32.05	0.9150	0.0500
313.15	47.80	0.9130	0.0520
313.15	64.45	0.9110	0.0540
313.15	75.39	0.9100	0.0550
313.15	94.44	0.9080	0.0560
313.15	110.27	0.9080	0.0570
323.15	3.41	0.9300	0.0340
323.15	20.58	0.9230	0.0420
323.15	38.28	0.9180	0.0460
323.15	46.68	0.9170	0.0470
323.15	52.53	0.9170	0.0480
323.15	65.17	0.9150	0.0490
323.15	80.30	0.9140	0.0500
323.15	101.83	0.9130	0.0520
333.15	3.17	0.9330	0.0310
333.15	12.84	0.9290	0.0350
333.15	35.87	0.9230	0.0420
333.15	53.14	0.9200	0.0440
333.15	62.24	0.9190	0.0450
333.15	73.55	0.9180	0.0460
333.15	84.64	0.9170	0.0470
333.15	100.39	0.9160	0.0480
303.15	1.41	0.8850	0.0570
303.15	3.93	0.8800	0.0620
303.15	6.96	0.8760	0.0660
303.15	11.84	0.8730	0.0690
303.15	18.65	0.8700	0.0720
303.15	30.05	0.8660	0.0760
303.15	51.18	0.8620	0.0810
303.15	76.44	0.8580	0.0850
303.15	105.81	0.8570	0.0860
313.15	2.35	0.8860	0.0550
313.15	9.31	0.8790	0.0630
313.15	14.44	0.8760	0.0660
313.15	17.66	0.8740	0.0680
313.15	23.24	0.8720	0.0700
313.15	41.52	0.8680	0.0740
313.15	59.20	0.8650	0.0770
313.15	75.39	0.8640	0.0790
313.15	92.08	0.8620	0.0800
323.15	2.22	0.8890	0.0520
323.15	3.50	0.8870	0.0540
323.15	14.27	0.8830	0.0580
323.15	28.99	0.8770	0.0650
323.15	41.77	0.8740	0.0680
323.15	56.94	0.8730	0.0690
323.15	74.16	0.8710	0.0710
323.15	94.98	0.8680	0.0740
333.15	2.48	0.8930	0.0480
333.15	6.27	0.8900	0.0510
333.15	17.52	0.8850	0.0560
333.15	32.37	0.8810	0.0610
333.15	47.11	0.8780	0.0640
333.15	62.72	0.8760	0.0660
333.15	77.52	0.8740	0.0680
333.15	121.88	0.8700	0.0720

Sources

• Vapor-liquid equilibrium measurement and ENRTL Modeling of CO2 absorption in aqueous hexamethylenediamine