Mixture of Triethylamine + Methyl Alcohol

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Fixed			Measured
Temperature, K - Gas	Mole fraction of Methyl Alcohol (2) - Gas	Mass density, kg/m3 - Gas	Viscosity, Pa*s - Gas
296.97	0.4998	2.1808	7.9130e-06
297.25	0.4996	0.6964	7.8530e-06
298.22	0.3322	1.2804	7.4760e-06
298.82	0.4996	0.6964	7.8870e-06
298.92	0.4982	1.1039	7.9140e-06
299.02	0.4999	0.6482	7.8650e-06
310.39	0.4996	0.6964	8.0550e-06
310.51	0.4998	2.1808	8.2590e-06
310.56	0.4999	0.6482	8.0250e-06
310.62	0.4982	1.1039	8.1470e-06
310.75	0.5035	1.5253	8.2350e-06
311.73	0.3322	1.2804	7.7120e-06
324.10	0.4998	2.1808	8.5390e-06
324.27	0.3322	1.2804	7.8520e-06
324.64	0.4996	0.6964	8.3380e-06
325.29	0.4982	1.1039	8.3370e-06
325.44	0.4999	0.6482	8.3670e-06
326.59	0.5035	1.5253	8.4760e-06
337.60	0.3322	1.2804	8.0720e-06
338.04	0.5035	1.5253	8.6260e-06
338.18	0.4982	1.1039	8.6320e-06
338.18	0.4999	0.6482	8.6930e-06
338.37	0.4996	0.6964	8.6950e-06
338.58	0.4998	2.1808	8.6900e-06
352.30	0.4996	0.6964	9.0390e-06
352.47	0.4999	0.6482	9.0530e-06
352.57	0.4982	1.1039	9.0090e-06
352.83	0.4998	2.1808	8.9490e-06
352.91	0.3322	1.2804	8.4410e-06
353.02	0.5035	1.5253	9.0260e-06
365.70	0.4998	2.1808	9.2810e-06
365.96	0.5035	1.5253	9.3490e-06
366.02	0.3322	1.2804	8.7660e-06
366.12	0.5035	1.5253	9.3630e-06
366.13	0.4999	0.6482	9.4110e-06
366.22	0.3322	1.2804	8.7470e-06
366.24	0.4996	0.6964	9.3880e-06
366.29	0.4982	1.1039	9.3530e-06
366.41	0.4998	2.1808	9.3070e-06
366.96	0.4999	0.6482	9.4150e-06
367.89	0.4982	1.1039	9.3810e-06
379.75	0.3322	1.2804	9.0750e-06
380.83	0.4998	2.1808	9.6810e-06
381.57	0.4999	0.6482	9.7930e-06
381.81	0.5035	1.5253	9.7700e-06
381.91	0.4982	1.1039	9.7580e-06
383.76	0.4996	0.6964	9.8280e-06
394.29	0.4998	2.1808	0.0000
394.84	0.5035	1.5253	0.0000
394.95	0.4996	0.6964	0.0000
394.98	0.3322	1.2804	9.4370e-06
395.04	0.4999	0.6482	0.0000
395.34	0.4982	1.1039	0.0000
408.74	0.3322	1.2804	9.7530e-06
409.01	0.4982	1.1039	0.0000
409.18	0.4998	2.1808	0.0000
409.61	0.4999	0.6482	0.0000
410.61	0.5035	1.5253	0.0000
410.75	0.4996	0.6964	0.0000
422.83	0.3322	1.2804	0.0000
423.21	0.5035	1.5253	0.0000
423.31	0.4996	0.6964	0.0000
423.64	0.4998	2.1808	0.0000
423.81	0.4982	1.1039	0.0000
425.55	0.4999	0.6482	0.0000
436.79	0.5035	1.5253	0.0000
436.89	0.4998	2.1808	0.0000
436.91	0.4996	0.6964	0.0000
437.47	0.4982	1.1039	0.0000
438.27	0.4999	0.6482	0.0000
441.21	0.3322	1.2804	0.0000
451.54	0.3322	1.2804	0.0000
451.60	0.5035	1.5253	0.0000
451.74	0.4982	1.1039	0.0000
452.02	0.4998	2.1808	0.0000
452.69	0.4996	0.6964	0.0000
453.25	0.4999	0.6482	0.0000
466.65	0.4998	2.1808	0.0000
466.76	0.5035	1.5253	0.0000
467.26	0.4982	1.1039	0.0000
467.40	0.3322	1.2804	0.0000
467.62	0.4999	0.6482	0.0000
480.98	0.3322	1.2804	0.0000
481.28	0.4982	1.1039	0.0000
481.51	0.4998	2.1808	0.0000
481.53	0.4996	0.6964	0.0000
482.14	0.4999	0.6482	0.0000
482.73	0.5035	1.5253	0.0000
494.94	0.4996	0.6964	0.0000
495.26	0.3322	1.2804	0.0000
495.28	0.4998	2.1808	0.0000
495.78	0.5035	1.5253	0.0000
496.37	0.4999	0.6482	0.0000
497.66	0.4982	1.1039	0.0000

Viscosity, Pa*s [ref]

Fixed			Measured
Temperature, K - Gas	Mole fraction of Methyl Alcohol (2) - Gas	Mass density, kg/m3 - Gas	Viscosity, Pa*s - Gas
296.97	0.4998	2.1808	7.9130e-06
297.25	0.4996	0.6964	7.8530e-06
298.22	0.3322	1.2804	7.4760e-06
298.82	0.4996	0.6964	7.8870e-06
298.92	0.4982	1.1039	7.9140e-06
299.02	0.4999	0.6482	7.8650e-06
310.39	0.4996	0.6964	8.0550e-06
310.51	0.4998	2.1808	8.2590e-06
310.56	0.4999	0.6482	8.0250e-06
310.62	0.4982	1.1039	8.1470e-06
310.75	0.5035	1.5253	8.2350e-06
311.73	0.3322	1.2804	7.7120e-06
324.10	0.4998	2.1808	8.5390e-06
324.27	0.3322	1.2804	7.8520e-06
324.64	0.4996	0.6964	8.3380e-06
325.29	0.4982	1.1039	8.3370e-06
325.44	0.4999	0.6482	8.3670e-06
326.59	0.5035	1.5253	8.4760e-06
337.60	0.3322	1.2804	8.0720e-06
338.04	0.5035	1.5253	8.6260e-06
338.18	0.4982	1.1039	8.6320e-06
338.18	0.4999	0.6482	8.6930e-06
338.37	0.4996	0.6964	8.6950e-06
338.58	0.4998	2.1808	8.6900e-06
352.30	0.4996	0.6964	9.0390e-06
352.47	0.4999	0.6482	9.0530e-06
352.57	0.4982	1.1039	9.0090e-06
352.83	0.4998	2.1808	8.9490e-06
352.91	0.3322	1.2804	8.4410e-06
353.02	0.5035	1.5253	9.0260e-06
365.70	0.4998	2.1808	9.2810e-06
365.96	0.5035	1.5253	9.3490e-06
366.02	0.3322	1.2804	8.7660e-06
366.12	0.5035	1.5253	9.3630e-06
366.13	0.4999	0.6482	9.4110e-06
366.22	0.3322	1.2804	8.7470e-06
366.24	0.4996	0.6964	9.3880e-06
366.29	0.4982	1.1039	9.3530e-06
366.41	0.4998	2.1808	9.3070e-06
366.96	0.4999	0.6482	9.4150e-06
367.89	0.4982	1.1039	9.3810e-06
379.75	0.3322	1.2804	9.0750e-06
380.83	0.4998	2.1808	9.6810e-06
381.57	0.4999	0.6482	9.7930e-06
381.81	0.5035	1.5253	9.7700e-06
381.91	0.4982	1.1039	9.7580e-06
383.76	0.4996	0.6964	9.8280e-06
394.29	0.4998	2.1808	0.0000
394.84	0.5035	1.5253	0.0000
394.95	0.4996	0.6964	0.0000
394.98	0.3322	1.2804	9.4370e-06
395.04	0.4999	0.6482	0.0000
395.34	0.4982	1.1039	0.0000
408.74	0.3322	1.2804	9.7530e-06
409.01	0.4982	1.1039	0.0000
409.18	0.4998	2.1808	0.0000
409.61	0.4999	0.6482	0.0000
410.61	0.5035	1.5253	0.0000
410.75	0.4996	0.6964	0.0000
422.83	0.3322	1.2804	0.0000
423.21	0.5035	1.5253	0.0000
423.31	0.4996	0.6964	0.0000
423.64	0.4998	2.1808	0.0000
423.81	0.4982	1.1039	0.0000
425.55	0.4999	0.6482	0.0000
436.79	0.5035	1.5253	0.0000
436.89	0.4998	2.1808	0.0000
436.91	0.4996	0.6964	0.0000
437.47	0.4982	1.1039	0.0000
438.27	0.4999	0.6482	0.0000
441.21	0.3322	1.2804	0.0000
451.54	0.3322	1.2804	0.0000
451.60	0.5035	1.5253	0.0000
451.74	0.4982	1.1039	0.0000
452.02	0.4998	2.1808	0.0000
452.69	0.4996	0.6964	0.0000
453.25	0.4999	0.6482	0.0000
466.65	0.4998	2.1808	0.0000
466.76	0.5035	1.5253	0.0000
467.26	0.4982	1.1039	0.0000
467.40	0.3322	1.2804	0.0000
467.62	0.4999	0.6482	0.0000
480.98	0.3322	1.2804	0.0000
481.28	0.4982	1.1039	0.0000
481.51	0.4998	2.1808	0.0000
481.53	0.4996	0.6964	0.0000
482.14	0.4999	0.6482	0.0000
482.73	0.5035	1.5253	0.0000
494.94	0.4996	0.6964	0.0000
495.26	0.3322	1.2804	0.0000
495.28	0.4998	2.1808	0.0000
495.78	0.5035	1.5253	0.0000
496.37	0.4999	0.6482	0.0000
497.66	0.4982	1.1039	0.0000

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Triethylamine (1) - Liquid	Mass density, kg/m3 - Liquid
0.1665	786.62
0.2201	786.484
0.3503	786.454
0.3885	786.356
0.4864	786.323
0.5092	786.248
0.6355	786.22
0.8289	786.124
0.9059	785.962
1.0319	785.895
1.2365	785.798

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Triethylamine (1) - Liquid	Mass density, kg/m3 - Liquid
0.1665	786.62
0.2201	786.484
0.3503	786.454
0.3885	786.356
0.4864	786.323
0.5092	786.248
0.6355	786.22
0.8289	786.124
0.9059	785.962
1.0319	785.895
1.2365	785.798

Sources

• The viscosity of the binary vapor mixture methanol triethylamine at low densities and in the saturated vapor phase of the vapor liquid equilibrium
• Partial molar volume of tertiary amines in methanol at T = 298.15 K. Solvation, shape and specific interactions