Mixture of Acetic acid, methyl ester + 2-Propanol, 1-methoxy-

Datasets

1. Mole fraction
2. ρ_l - Mass density, kg/m3
3. c_sound,fluid - Speed of Sound, m/s

Mole fraction of Acetic acid, methyl ester (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Acetic acid, methyl ester (1) - Liquid	Mole fraction of Acetic acid, methyl ester (1) - Gas
330.50	1.0000	1.0000
331.00	0.9909	0.9987
331.50	0.9699	0.9954
332.10	0.9468	0.9923
332.60	0.9244	0.9892
333.40	0.8900	0.9845
334.10	0.8624	0.9818
334.70	0.8370	0.9786
336.50	0.7657	0.9687
337.30	0.7343	0.9639
338.40	0.6973	0.9586
338.60	0.6898	0.9572
339.40	0.6653	0.9528
340.80	0.6223	0.9437
340.70	0.6244	0.9444
343.10	0.5596	0.9286
345.10	0.5111	0.9157
349.10	0.4275	0.8851
351.70	0.3803	0.8619
353.90	0.3449	0.8406
357.70	0.2858	0.7930
364.40	0.2265	0.7213
368.20	0.1728	0.6481
373.60	0.1261	0.5404
379.20	0.0836	0.4128
380.90	0.0717	0.3698
384.10	0.0511	0.2862
388.20	0.0260	0.1611
390.10	0.0153	0.0991
392.90	0.0004	0.0033
393.30	0.0000	0.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	940.883
288.15	0.0207	940.053
288.15	0.0464	939.345
288.15	0.1088	937.89
288.15	0.1939	935.816
288.15	0.2843	933.707
288.15	0.3772	932.0
288.15	0.4897	930.444
288.15	0.5760	929.443
288.15	0.7024	928.089
288.15	0.7922	927.337
288.15	0.8772	926.778
288.15	0.9355	926.432
288.15	0.9667	926.133
288.15	1.0000	925.9
293.15	0.0000	934.389
293.15	0.0207	933.582
293.15	0.0464	932.934
293.15	0.1088	931.615
293.15	0.1939	929.703
293.15	0.2843	927.777
293.15	0.3772	926.311
293.15	0.4897	925.001
293.15	0.5760	924.044
293.15	0.7024	922.902
293.15	0.7922	922.299
293.15	0.8772	921.881
293.15	0.9355	921.626
293.15	0.9667	921.378
293.15	1.0000	921.196
298.15	0.0000	927.817
298.15	0.0207	927.069
298.15	0.0464	926.466
298.15	0.1088	925.284
298.15	0.1939	923.547
298.15	0.2843	921.803
298.15	0.3772	920.59
298.15	0.4897	919.404
298.15	0.5760	918.604
298.15	0.7024	917.676
298.15	0.7922	917.224
298.15	0.8772	916.944
298.15	0.9355	916.78
298.15	0.9667	916.583
298.15	1.0000	916.449
303.15	0.0000	921.188
303.15	0.0207	920.495
303.15	0.0464	919.946
303.15	0.1088	918.901
303.15	0.1939	917.338
303.15	0.2843	915.78
303.15	0.3772	914.766
303.15	0.4897	913.8
303.15	0.5760	913.22
303.15	0.7024	912.405
303.15	0.7922	912.101
303.15	0.8772	911.965
303.15	0.9355	911.892
303.15	0.9667	911.739
303.15	1.0000	911.655
308.15	0.0000	914.498
308.15	0.0207	913.861
308.15	0.0464	913.38
308.15	0.1088	912.46
308.15	0.1939	911.075
308.15	0.2843	909.706
308.15	0.3772	908.911
308.15	0.4897	908.176
308.15	0.5760	907.711
308.15	0.7024	907.151
308.15	0.7922	906.934
308.15	0.8772	906.94
308.15	0.9355	906.957
308.15	0.9667	906.849
308.15	1.0000	906.816

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0000	1200.38
288.15	0.0207	1202.73
288.15	0.0464	1204.44
288.15	0.1088	1209.23
288.15	0.1939	1215.18
288.15	0.2843	1221.96
288.15	0.3772	1229.5
288.15	0.4897	1240.5
288.15	0.5760	1249.8
288.15	0.7024	1263.31
288.15	0.7922	1273.63
288.15	0.8772	1284.13
288.15	0.9355	1291.02
288.15	0.9667	1294.47
288.15	1.0000	1298.14
293.15	0.0000	1178.95
293.15	0.0207	1180.34
293.15	0.0464	1182.35
293.15	0.1088	1187.72
293.15	0.1939	1193.7
293.15	0.2843	1200.89
293.15	0.3772	1209.01
293.15	0.4897	1220.8
293.15	0.5760	1230.25
293.15	0.7024	1244.0
293.15	0.7922	1254.7
293.15	0.8772	1265.55
293.15	0.9355	1272.67
293.15	0.9667	1276.26
293.15	1.0000	1280.08
298.15	0.0000	1155.93
298.15	0.0207	1157.5
298.15	0.0464	1159.18
298.15	0.1088	1165.35
298.15	0.1939	1171.76
298.15	0.2843	1179.38
298.15	0.3772	1188.04
298.15	0.4897	1200.02
298.15	0.5760	1209.99
298.15	0.7024	1224.24
298.15	0.7922	1235.33
298.15	0.8772	1246.5
298.15	0.9355	1253.87
298.15	0.9667	1257.61
298.15	1.0000	1261.54
303.15	0.0000	1132.98
303.15	0.0207	1134.72
303.15	0.0464	1136.54
303.15	0.1088	1143.03
303.15	0.1939	1149.87
303.15	0.2843	1157.93
303.15	0.3772	1166.79
303.15	0.4897	1179.4
303.15	0.5760	1189.68
303.15	0.7024	1204.55
303.15	0.7922	1215.98
303.15	0.8772	1227.52
303.15	0.9355	1235.14
303.15	0.9667	1238.97
303.15	1.0000	1243.03
308.15	0.0000	1110.02
308.15	0.0207	1111.93
308.15	0.0464	1114.41
308.15	0.1088	1120.75
308.15	0.1939	1128.01
308.15	0.2843	1136.48
308.15	0.3772	1145.5
308.15	0.4897	1159.01
308.15	0.5760	1169.61
308.15	0.7024	1184.88
308.15	0.7922	1196.66
308.15	0.8772	1208.53
308.15	0.9355	1216.39
308.15	0.9667	1220.3
308.15	1.0000	1224.5

Sources

• Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
• Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K

Note: These property values are available through the Cheméo API. A free account gives you an access key.