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

Datasets

1. P_vap - Vapor or sublimation pressure, kPa
2. ρ_l - Mass density, kg/m3
3. c_sound,fluid - Speed of Sound, m/s

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetic acid, butyl ester (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
423.15	1.0000	191.33
423.15	0.9694	193.81
423.15	0.9416	195.37
423.15	0.9138	198.87
423.15	0.8878	201.06
423.15	0.8615	204.14
423.15	0.8048	208.57
423.15	0.7523	213.12
423.15	0.6947	217.87
423.15	0.6439	221.00
423.15	0.5955	223.73
423.15	0.5437	226.11
423.15	0.5097	228.79
423.15	0.4921	228.62
423.15	0.4599	231.60
423.15	0.4413	231.39
423.15	0.4086	233.18
423.15	0.3568	234.28
423.15	0.3027	235.24
423.15	0.2514	236.06
423.15	0.2019	236.53
423.15	0.1530	236.09
423.15	0.1048	235.79
423.15	0.0779	234.74
423.15	0.0474	234.14
423.15	0.0188	233.33
423.15	0.0000	231.95
473.15	1.0000	583.23
473.15	0.9734	589.50
473.15	0.9487	596.47
473.15	0.9249	604.12
473.15	0.9007	609.08
473.15	0.8500	625.35
473.15	0.7986	638.18
473.15	0.7478	650.93
473.15	0.6949	662.66
473.15	0.6436	672.38
473.15	0.5914	683.27
473.15	0.5726	684.93
473.15	0.5387	693.13
473.15	0.5227	692.30
473.15	0.4709	700.71
473.15	0.4198	707.06
473.15	0.3668	713.47
473.15	0.3152	718.92
473.15	0.2610	724.85
473.15	0.2084	729.53
473.15	0.1543	734.08
473.15	0.1021	736.50
473.15	0.0762	739.12
473.15	0.0499	738.57
473.15	0.0244	739.81
473.15	0.0000	739.81

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	885.958
288.15	0.0200	886.462
288.15	0.0317	886.612
288.15	0.0966	888.134
288.15	0.1861	890.343
288.15	0.3019	893.536
288.15	0.3836	896.154
288.15	0.5168	901.159
288.15	0.5990	904.586
288.15	0.6873	908.54
288.15	0.7896	913.679
288.15	0.8984	919.722
288.15	0.9399	922.264
288.15	0.9711	924.228
288.15	1.0000	925.9
293.15	0.0000	880.87
293.15	0.0200	881.348
293.15	0.0317	881.507
293.15	0.0966	883.029
293.15	0.1861	885.237
293.15	0.3019	888.454
293.15	0.3836	891.087
293.15	0.5168	896.138
293.15	0.5990	899.602
293.15	0.6873	903.602
293.15	0.7896	908.805
293.15	0.8984	914.933
293.15	0.9399	917.503
293.15	0.9711	919.495
293.15	1.0000	921.196
298.15	0.0000	875.739
298.15	0.0200	876.219
298.15	0.0317	876.372
298.15	0.0966	877.897
298.15	0.1861	880.108
298.15	0.3019	883.34
298.15	0.3836	885.993
298.15	0.5168	891.082
298.15	0.5990	894.583
298.15	0.6873	898.627
298.15	0.7896	903.889
298.15	0.8984	910.096
298.15	0.9399	912.702
298.15	0.9711	914.726
298.15	1.0000	916.449
303.15	0.0000	870.584
303.15	0.0200	871.064
303.15	0.0317	871.218
303.15	0.0966	872.738
303.15	0.1861	874.954
303.15	0.3019	878.199
303.15	0.3836	880.868
303.15	0.5168	885.995
303.15	0.5990	889.525
303.15	0.6873	893.613
303.15	0.7896	898.935
303.15	0.8984	905.216
303.15	0.9399	907.856
303.15	0.9711	909.906
303.15	1.0000	911.655
308.15	0.0000	865.41
308.15	0.0200	865.886
308.15	0.0317	866.038
308.15	0.0966	867.556
308.15	0.1861	869.775
308.15	0.3019	873.032
308.15	0.3836	875.714
308.15	0.5168	880.877
308.15	0.5990	884.435
308.15	0.6873	888.561
308.15	0.7896	893.941
308.15	0.8984	900.292
308.15	0.9399	902.967
308.15	0.9711	905.043
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	1233.32
288.15	0.0200	1233.96
288.15	0.0317	1233.8
288.15	0.0966	1235.72
288.15	0.1861	1238.11
288.15	0.3019	1241.72
288.15	0.3836	1245.07
288.15	0.5168	1252.55
288.15	0.5990	1258.06
288.15	0.6873	1264.78
288.15	0.7896	1274.11
288.15	0.8984	1285.81
288.15	0.9399	1290.83
288.15	0.9711	1294.81
288.15	1.0000	1298.14
293.15	0.0000	1213.05
293.15	0.0200	1213.66
293.15	0.0317	1213.7
293.15	0.0966	1215.63
293.15	0.1861	1218.11
293.15	0.3019	1221.97
293.15	0.3836	1225.42
293.15	0.5168	1233.18
293.15	0.5990	1238.87
293.15	0.6873	1245.8
293.15	0.7896	1255.41
293.15	0.8984	1267.4
293.15	0.9399	1272.55
293.15	0.9711	1276.61
293.15	1.0000	1280.08
298.15	0.0000	1192.35
298.15	0.0200	1193.01
298.15	0.0317	1193.02
298.15	0.0966	1195.1
298.15	0.1861	1197.75
298.15	0.3019	1201.76
298.15	0.3836	1205.39
298.15	0.5168	1213.4
298.15	0.5990	1219.26
298.15	0.6873	1226.39
298.15	0.7896	1236.22
298.15	0.8984	1248.51
298.15	0.9399	1253.81
298.15	0.9711	1258.0
298.15	1.0000	1261.54
303.15	0.0000	1171.79
303.15	0.0200	1172.5
303.15	0.0317	1172.54
303.15	0.0966	1174.69
303.15	0.1861	1177.5
303.15	0.3019	1181.7
303.15	0.3836	1185.46
303.15	0.5168	1193.73
303.15	0.5990	1199.72
303.15	0.6873	1207.04
303.15	0.7896	1217.12
303.15	0.8984	1229.69
303.15	0.9399	1235.11
303.15	0.9711	1239.38
303.15	1.0000	1243.03
308.15	0.0000	1151.35
308.15	0.0200	1152.09
308.15	0.0317	1152.13
308.15	0.0966	1154.39
308.15	0.1861	1157.36
308.15	0.3019	1161.73
308.15	0.3836	1165.59
308.15	0.5168	1174.11
308.15	0.5990	1180.23
308.15	0.6873	1187.72
308.15	0.7896	1198.03
308.15	0.8984	1210.86
308.15	0.9399	1216.41
308.15	0.9711	1220.78
308.15	1.0000	1224.5

Sources

• 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
• Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation

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