Datasets
-
Mole fraction (4)
-
Liquid-liquid equilibrium temperature, K (4)
-
Interfacial tension, N/m (6)
-
ρl - Mass density, kg/m3 (8)
Mole fraction of Heptane (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Heptane (2) - Liquid mixture 1 |
313.20 |
101.00 |
0.0280 |
Mole fraction of Heptane (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Heptane (2) - Liquid mixture 2 |
313.20 |
101.00 |
0.9820 |
Mole fraction of Heptane (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Heptane (2) - Liquid mixture 1 |
313.20 |
101.00 |
0.0280 |
Mole fraction of Heptane (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Heptane (2) - Liquid mixture 2 |
313.20 |
101.00 |
0.9820 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.0405 |
285.97 |
0.0504 |
293.12 |
0.0600 |
297.13 |
0.0709 |
301.58 |
0.0755 |
304.07 |
0.1007 |
311.83 |
0.1299 |
320.41 |
0.1495 |
323.51 |
0.1716 |
327.06 |
0.1856 |
328.49 |
0.2033 |
330.77 |
0.2198 |
332.21 |
0.2227 |
332.50 |
0.2509 |
335.46 |
0.2782 |
337.18 |
0.3056 |
338.85 |
0.3236 |
340.07 |
0.3516 |
340.85 |
0.3833 |
342.06 |
0.4097 |
342.57 |
0.4231 |
342.69 |
0.4524 |
342.95 |
0.4775 |
343.08 |
0.5045 |
343.21 |
0.5324 |
343.32 |
0.5535 |
343.35 |
0.5613 |
343.36 |
0.5770 |
343.27 |
0.5963 |
343.18 |
0.6209 |
342.85 |
0.6485 |
342.39 |
0.6746 |
341.98 |
0.7004 |
340.90 |
0.7238 |
339.93 |
0.7259 |
339.83 |
0.7538 |
337.65 |
0.7770 |
335.21 |
0.8009 |
332.35 |
0.8205 |
329.41 |
0.8316 |
327.47 |
0.8441 |
324.80 |
0.8459 |
324.28 |
0.8464 |
324.17 |
0.8509 |
323.05 |
0.8596 |
321.08 |
0.8759 |
316.26 |
0.8907 |
311.34 |
0.9054 |
304.87 |
0.9170 |
299.08 |
0.9232 |
295.82 |
0.9269 |
293.20 |
0.9322 |
289.26 |
0.9359 |
287.24 |
0.9415 |
282.97 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.2648 |
336.67 |
0.3056 |
338.74 |
0.3529 |
340.56 |
0.3693 |
341.15 |
0.4034 |
341.76 |
0.4243 |
342.08 |
0.4472 |
342.33 |
0.4880 |
342.48 |
0.5092 |
342.63 |
0.5446 |
342.56 |
0.5775 |
342.37 |
0.5984 |
342.30 |
0.6181 |
342.22 |
0.6457 |
341.55 |
0.6915 |
340.28 |
0.6916 |
340.42 |
0.7489 |
337.31 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.0405 |
285.97 |
0.0504 |
293.12 |
0.0600 |
297.13 |
0.0709 |
301.58 |
0.0755 |
304.07 |
0.1007 |
311.83 |
0.1299 |
320.41 |
0.1495 |
323.51 |
0.1716 |
327.06 |
0.1856 |
328.49 |
0.2033 |
330.77 |
0.2198 |
332.21 |
0.2227 |
332.50 |
0.2509 |
335.46 |
0.2782 |
337.18 |
0.3056 |
338.85 |
0.3236 |
340.07 |
0.3516 |
340.85 |
0.3833 |
342.06 |
0.4097 |
342.57 |
0.4231 |
342.69 |
0.4524 |
342.95 |
0.4775 |
343.08 |
0.5045 |
343.21 |
0.5324 |
343.32 |
0.5535 |
343.35 |
0.5613 |
343.36 |
0.5770 |
343.27 |
0.5963 |
343.18 |
0.6209 |
342.85 |
0.6485 |
342.39 |
0.6746 |
341.98 |
0.7004 |
340.90 |
0.7238 |
339.93 |
0.7259 |
339.83 |
0.7538 |
337.65 |
0.7770 |
335.21 |
0.8009 |
332.35 |
0.8205 |
329.41 |
0.8316 |
327.47 |
0.8441 |
324.80 |
0.8459 |
324.28 |
0.8464 |
324.17 |
0.8509 |
323.05 |
0.8596 |
321.08 |
0.8759 |
316.26 |
0.8907 |
311.34 |
0.9054 |
304.87 |
0.9170 |
299.08 |
0.9232 |
295.82 |
0.9269 |
293.20 |
0.9322 |
289.26 |
0.9359 |
287.24 |
0.9415 |
282.97 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.2648 |
336.67 |
0.3056 |
338.74 |
0.3529 |
340.56 |
0.3693 |
341.15 |
0.4034 |
341.76 |
0.4243 |
342.08 |
0.4472 |
342.33 |
0.4880 |
342.48 |
0.5092 |
342.63 |
0.5446 |
342.56 |
0.5775 |
342.37 |
0.5984 |
342.30 |
0.6181 |
342.22 |
0.6457 |
341.55 |
0.6915 |
340.28 |
0.6916 |
340.42 |
0.7489 |
337.31 |
Interfacial tension, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Heptane (2) - Liquid |
Interfacial tension, N/m - Liquid |
298.15 |
0.0000 |
0.0360 |
298.15 |
0.0160 |
0.0341 |
298.15 |
0.0250 |
0.0322 |
298.15 |
0.0300 |
0.0314 |
298.15 |
0.0460 |
0.0287 |
298.15 |
0.0560 |
0.0277 |
298.15 |
0.0570 |
0.0274 |
298.15 |
0.0580 |
0.0270 |
298.15 |
0.9440 |
0.0205 |
298.15 |
0.9450 |
0.0205 |
298.15 |
0.9590 |
0.0204 |
298.15 |
0.9750 |
0.0204 |
298.15 |
0.9840 |
0.0203 |
298.15 |
1.0000 |
0.0198 |
318.15 |
0.0000 |
0.0334 |
318.15 |
0.0160 |
0.0319 |
318.15 |
0.0250 |
0.0311 |
318.15 |
0.0300 |
0.0304 |
318.15 |
0.0370 |
0.0292 |
318.15 |
0.0460 |
0.0280 |
318.15 |
0.0560 |
0.0270 |
318.15 |
0.0570 |
0.0270 |
318.15 |
0.0580 |
0.0266 |
318.15 |
0.0600 |
0.0262 |
318.15 |
0.0800 |
0.0243 |
318.15 |
0.1000 |
0.0222 |
318.15 |
0.8780 |
0.0189 |
318.15 |
0.9100 |
0.0186 |
318.15 |
0.9440 |
0.0188 |
318.15 |
0.9450 |
0.0187 |
318.15 |
0.9590 |
0.0188 |
318.15 |
0.9750 |
0.0182 |
318.15 |
0.9840 |
0.0181 |
318.15 |
1.0000 |
0.0179 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
297.83 |
0.0024 |
308.00 |
0.0019 |
317.75 |
0.0013 |
328.15 |
0.0007 |
297.83 |
0.0024 |
308.00 |
0.0019 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
297.83 |
0.0025 |
302.83 |
0.0022 |
307.85 |
0.0019 |
312.85 |
0.0016 |
317.86 |
0.0013 |
322.86 |
0.0009 |
327.88 |
0.0007 |
332.88 |
0.0004 |
334.87 |
0.0003 |
336.86 |
0.0002 |
337.88 |
0.0002 |
338.88 |
0.0001 |
339.87 |
0.0001 |
340.87 |
0.0000 |
341.25 |
0.0000 |
341.88 |
0.0000 |
342.18 |
0.0000 |
Interfacial tension, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Heptane (2) - Liquid |
Interfacial tension, N/m - Liquid |
298.15 |
0.0000 |
0.0360 |
298.15 |
0.0160 |
0.0341 |
298.15 |
0.0250 |
0.0322 |
298.15 |
0.0300 |
0.0314 |
298.15 |
0.0460 |
0.0287 |
298.15 |
0.0560 |
0.0277 |
298.15 |
0.0570 |
0.0274 |
298.15 |
0.0580 |
0.0270 |
298.15 |
0.9440 |
0.0205 |
298.15 |
0.9450 |
0.0205 |
298.15 |
0.9590 |
0.0204 |
298.15 |
0.9750 |
0.0204 |
298.15 |
0.9840 |
0.0203 |
298.15 |
1.0000 |
0.0198 |
318.15 |
0.0000 |
0.0334 |
318.15 |
0.0160 |
0.0319 |
318.15 |
0.0250 |
0.0311 |
318.15 |
0.0300 |
0.0304 |
318.15 |
0.0370 |
0.0292 |
318.15 |
0.0460 |
0.0280 |
318.15 |
0.0560 |
0.0270 |
318.15 |
0.0570 |
0.0270 |
318.15 |
0.0580 |
0.0266 |
318.15 |
0.0600 |
0.0262 |
318.15 |
0.0800 |
0.0243 |
318.15 |
0.1000 |
0.0222 |
318.15 |
0.8780 |
0.0189 |
318.15 |
0.9100 |
0.0186 |
318.15 |
0.9440 |
0.0188 |
318.15 |
0.9450 |
0.0187 |
318.15 |
0.9590 |
0.0188 |
318.15 |
0.9750 |
0.0182 |
318.15 |
0.9840 |
0.0181 |
318.15 |
1.0000 |
0.0179 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
297.83 |
0.0024 |
308.00 |
0.0019 |
317.75 |
0.0013 |
328.15 |
0.0007 |
297.83 |
0.0024 |
308.00 |
0.0019 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
297.83 |
0.0025 |
302.83 |
0.0022 |
307.85 |
0.0019 |
312.85 |
0.0016 |
317.86 |
0.0013 |
322.86 |
0.0009 |
327.88 |
0.0007 |
332.88 |
0.0004 |
334.87 |
0.0003 |
336.86 |
0.0002 |
337.88 |
0.0002 |
338.88 |
0.0001 |
339.87 |
0.0001 |
340.87 |
0.0000 |
341.25 |
0.0000 |
341.88 |
0.0000 |
342.18 |
0.0000 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Heptane (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
944.072 |
298.15 |
0.0160 |
937.085 |
298.15 |
0.0250 |
933.113 |
298.15 |
0.0300 |
930.536 |
298.15 |
0.0370 |
927.759 |
298.15 |
0.0460 |
923.761 |
298.15 |
0.0560 |
919.794 |
298.15 |
0.0570 |
919.14 |
298.15 |
0.0580 |
918.702 |
298.15 |
0.9350 |
687.975 |
298.15 |
0.9440 |
686.984 |
298.15 |
0.9450 |
686.853 |
298.15 |
0.9590 |
684.733 |
298.15 |
0.9750 |
682.892 |
298.15 |
0.9840 |
681.827 |
298.15 |
1.0000 |
679.788 |
318.15 |
0.0000 |
924.984 |
318.15 |
0.0160 |
918.051 |
318.15 |
0.0250 |
914.603 |
318.15 |
0.0300 |
911.498 |
318.15 |
0.0370 |
908.897 |
318.15 |
0.0460 |
905.072 |
318.15 |
0.0560 |
901.036 |
318.15 |
0.0570 |
900.33 |
318.15 |
0.0580 |
899.742 |
318.15 |
0.0600 |
899.281 |
318.15 |
0.0800 |
891.094 |
318.15 |
0.1000 |
882.094 |
318.15 |
0.9350 |
670.394 |
318.15 |
0.9440 |
669.492 |
318.15 |
0.9450 |
669.302 |
318.15 |
0.9590 |
667.371 |
318.15 |
0.9750 |
665.45 |
318.15 |
0.9840 |
664.351 |
318.15 |
1.0000 |
662.387 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 1 |
297.83 |
689.08 |
907.04 |
308.00 |
684.51 |
888.35 |
317.75 |
680.13 |
868.1 |
328.15 |
684.46 |
839.73 |
Mass density, kg/m3
[ref]
Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
298.21 |
689.3 |
303.17 |
686.3 |
308.12 |
684.4 |
313.10 |
683.1 |
318.05 |
679.9 |
323.02 |
682.0 |
332.94 |
685.7 |
335.41 |
688.4 |
337.89 |
693.2 |
338.89 |
695.6 |
339.89 |
699.5 |
340.36 |
700.5 |
340.48 |
702.3 |
340.48 |
700.8 |
340.87 |
704.3 |
340.88 |
702.3 |
340.88 |
703.0 |
341.18 |
704.4 |
341.46 |
705.9 |
341.46 |
705.3 |
341.85 |
705.6 |
341.95 |
708.5 |
342.05 |
708.2 |
342.16 |
710.3 |
342.16 |
710.9 |
342.25 |
712.5 |
342.25 |
712.3 |
342.35 |
717.1 |
342.40 |
719.0 |
342.45 |
720.2 |
342.51 |
721.8 |
342.56 |
719.6 |
342.60 |
725.8 |
342.64 |
725.3 |
342.64 |
725.4 |
Mass density, kg/m3
[ref]
Temperature, K - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
298.21 |
906.0 |
303.17 |
897.3 |
308.12 |
888.3 |
313.10 |
878.5 |
318.05 |
867.9 |
323.02 |
855.7 |
332.94 |
825.6 |
335.41 |
815.8 |
337.89 |
805.2 |
338.89 |
799.4 |
339.89 |
792.8 |
340.36 |
788.4 |
340.48 |
787.7 |
340.48 |
787.7 |
340.87 |
784.9 |
340.88 |
783.8 |
340.88 |
783.8 |
341.18 |
780.8 |
341.46 |
777.1 |
341.46 |
777.1 |
341.85 |
780.2 |
341.95 |
778.4 |
342.05 |
776.7 |
342.16 |
774.9 |
342.16 |
775.5 |
342.25 |
773.5 |
342.25 |
773.5 |
342.35 |
767.2 |
342.40 |
765.9 |
342.45 |
764.4 |
342.51 |
761.7 |
342.56 |
758.6 |
342.60 |
755.8 |
342.64 |
750.6 |
342.64 |
750.6 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Heptane (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
944.072 |
298.15 |
0.0160 |
937.085 |
298.15 |
0.0250 |
933.113 |
298.15 |
0.0300 |
930.536 |
298.15 |
0.0370 |
927.759 |
298.15 |
0.0460 |
923.761 |
298.15 |
0.0560 |
919.794 |
298.15 |
0.0570 |
919.14 |
298.15 |
0.0580 |
918.702 |
298.15 |
0.9350 |
687.975 |
298.15 |
0.9440 |
686.984 |
298.15 |
0.9450 |
686.853 |
298.15 |
0.9590 |
684.733 |
298.15 |
0.9750 |
682.892 |
298.15 |
0.9840 |
681.827 |
298.15 |
1.0000 |
679.788 |
318.15 |
0.0000 |
924.984 |
318.15 |
0.0160 |
918.051 |
318.15 |
0.0250 |
914.603 |
318.15 |
0.0300 |
911.498 |
318.15 |
0.0370 |
908.897 |
318.15 |
0.0460 |
905.072 |
318.15 |
0.0560 |
901.036 |
318.15 |
0.0570 |
900.33 |
318.15 |
0.0580 |
899.742 |
318.15 |
0.0600 |
899.281 |
318.15 |
0.0800 |
891.094 |
318.15 |
0.1000 |
882.094 |
318.15 |
0.9350 |
670.394 |
318.15 |
0.9440 |
669.492 |
318.15 |
0.9450 |
669.302 |
318.15 |
0.9590 |
667.371 |
318.15 |
0.9750 |
665.45 |
318.15 |
0.9840 |
664.351 |
318.15 |
1.0000 |
662.387 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 1 |
297.83 |
689.08 |
907.04 |
308.00 |
684.51 |
888.35 |
317.75 |
680.13 |
868.1 |
328.15 |
684.46 |
839.73 |
Mass density, kg/m3
[ref]
Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
298.21 |
689.3 |
303.17 |
686.3 |
308.12 |
684.4 |
313.10 |
683.1 |
318.05 |
679.9 |
323.02 |
682.0 |
332.94 |
685.7 |
335.41 |
688.4 |
337.89 |
693.2 |
338.89 |
695.6 |
339.89 |
699.5 |
340.36 |
700.5 |
340.48 |
702.3 |
340.48 |
700.8 |
340.87 |
704.3 |
340.88 |
702.3 |
340.88 |
703.0 |
341.18 |
704.4 |
341.46 |
705.9 |
341.46 |
705.3 |
341.85 |
705.6 |
341.95 |
708.5 |
342.05 |
708.2 |
342.16 |
710.3 |
342.16 |
710.9 |
342.25 |
712.5 |
342.25 |
712.3 |
342.35 |
717.1 |
342.40 |
719.0 |
342.45 |
720.2 |
342.51 |
721.8 |
342.56 |
719.6 |
342.60 |
725.8 |
342.64 |
725.3 |
342.64 |
725.4 |
Mass density, kg/m3
[ref]
Temperature, K - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
298.21 |
906.0 |
303.17 |
897.3 |
308.12 |
888.3 |
313.10 |
878.5 |
318.05 |
867.9 |
323.02 |
855.7 |
332.94 |
825.6 |
335.41 |
815.8 |
337.89 |
805.2 |
338.89 |
799.4 |
339.89 |
792.8 |
340.36 |
788.4 |
340.48 |
787.7 |
340.48 |
787.7 |
340.87 |
784.9 |
340.88 |
783.8 |
340.88 |
783.8 |
341.18 |
780.8 |
341.46 |
777.1 |
341.46 |
777.1 |
341.85 |
780.2 |
341.95 |
778.4 |
342.05 |
776.7 |
342.16 |
774.9 |
342.16 |
775.5 |
342.25 |
773.5 |
342.25 |
773.5 |
342.35 |
767.2 |
342.40 |
765.9 |
342.45 |
764.4 |
342.51 |
761.7 |
342.56 |
758.6 |
342.60 |
755.8 |
342.64 |
750.6 |
342.64 |
750.6 |
Sources