资源描述
Isobaric P-T-X-Y Data : ETHANOL + WATER at 760mmHg
Reference
Rieder,R.M. and A.R.Thompson, I&EC, 41, 2905 (1949)
Method
Number of Data Points = 36
T,deg.C
P,mmHg
X
Y
T Err
P Err
X Err
Y Err
100.0
760
0
0
+-0.2
99.3
760
0.0028
0.032
+-0.2
96.9
760
0.0118
0.113
+-0.2
96.0
760
0.0137
0.157
+-0.2
96.0
760
0.0144
0.135
+-0.2
95.6
760
0.0176
0.156
+-0.2
94.8
760
0.0222
0.186
+-0.2
93.8
760
0.0246
0.212
+-0.2
93.5
760
0.0302
0.231
+-0.2
92.9
760
0.0331
0.248
+-0.2
90.5
760
0.0519
0.318
+-0.2
90.5
760
0.0530
0.314
+-0.2
89.4
760
0.0625
0.339
+-0.2
88.4
760
0.0673
0.370
+-0.2
88.6
760
0.0715
0.362
+-0.2
87.2
760
0.0871
0.406
+-0.2
85.4
760
0.126
0.468
+-0.2
84.5
760
0.143
0.487
+-0.2
84.0
760
0.172
0.505
+-0.2
83.4
760
0.206
0.530
+-0.2
83.0
760
0.210
0.527
+-0.2
82.3
760
0.255
0.552
+-0.2
82.0
760
0.284
0.567
+-0.2
81.4
760
0.321
0.586
+-0.2
81.5
760
0.324
0.583
+-0.2
81.2
760
0.345
0.591
+-0.2
80.9
760
0.405
0.614
+-0.2
80.5
760
0.430
0.628
+-0.2
80.2
760
0.449
0.633
+-0.2
80.0
760
0.506
0.661
+-0.2
79.5
760
0.545
0.673
+-0.2
78.8
760
0.663
0.733
+-0.2
78.5
760
0.735
0.776
+-0.2
78.4
760
0.804
0.815
+-0.2
78.3
760
0.917
0.906
+-0.2
78.3
760
1.000
1.000
+-0.2
Isobaric P-T-X Data : ETHANOL + WATER
Reference
KENJI OCHI and KAZUO KOJIMA, J. Chem. Eng. Japan, 20, 6 (1987)
Method
EBULLIOMETRIC METHOD
Number of Data Points = 22
T,K
P,kPa
X
Y
T Err
P Err
X Err
Y Err
373.13
101.325
0.000070
373.12
101.325
0.000090
373.11
101.325
0.000102
373.11
101.325
0.000148
373.10
101.325
0.000169
373.07
101.325
0.000238
373.04
101.325
0.000317
373.03
101.325
0.000326
373.00
101.325
0.000436
372.97
101.325
0.000560
372.93
101.325
0.000602
372.85
101.325
0.000854
372.78
101.325
0.000963
372.65
101.325
0.00132
372.55
101.325
0.00161
372.25
101.325
0.00265
372.02
101.325
0.00330
371.70
101.325
0.00447
371.54
101.325
0.00499
371.00
101.325
0.00638
370.69
101.325
0.00756
370.30
101.325
0.00858
Isothermal P-T-X Data : ETHANOL + WATER at 150.5C
Reference
KOLBE,B. and J.GMEHLING, Fluid Phase Equilib., 23, 213 (1985)
Method
STATIC METHOD
Number of Data Points = 32
T,deg.C
P,bar
X
Y
T Err
P Err
X Err
Y Err
150.5
5.1737
0.00732
+-0.1
150.5
5.3805
0.01210
+-0.1
150.5
5.6954
0.02040
+-0.1
150.5
6.0277
0.03012
+-0.1
150.5
6.4920
0.04669
+-0.1
150.5
7.0251
0.07205
+-0.1
150.5
7.3942
0.09619
+-0.1
150.5
7.8150
0.13497
+-0.1
150.5
7.9785
0.15447
+-0.1
150.5
8.1250
0.17469
+-0.1
150.5
8.2394
0.19253
+-0.1
150.5
8.5110
0.24227
+-0.1
150.5
8.7156
0.28690
+-0.1
150.5
8.5599
0.25252
+-0.1
150.5
8.7775
0.30256
+-0.1
150.5
8.9686
0.35235
+-0.1
150.5
9.1413
0.40204
+-0.1
150.5
9.3007
0.45219
+-0.1
150.5
9.4431
0.50193
+-0.1
150.5
9.5745
0.55175
+-0.1
150.5
9.6908
0.60191
+-0.1
150.5
9.7896
0.65002
+-0.1
150.5
9.8763
0.70150
+-0.1
150.5
9.9412
0.75054
+-0.1
150.5
9.9881
0.80043
+-0.1
150.5
10.0107
0.85005
+-0.1
150.5
10.0130
0.87336
+-0.1
150.5
10.0088
0.90035
+-0.1
150.5
9.9961
0.92868
+-0.1
150.5
9.9759
0.95460
+-0.1
150.5
9.9445
0.98400
+-0.1
150.5
9.9251
0.99751
+-0.1
Isothermal P-T-X Data : ETHANOL + WATER at 90.1C
Reference
KOLBE,B. and J.GMEHLING, Fluid Phase Equilib., 23, 213 (1985)
Method
STATIC METHOD
Number of Data Points = 23
T,deg.C
P,bar
X
Y
T Err
P Err
X Err
Y Err
90.1
1.0413
0.05444
+-0.1
90.1
1.2121
0.11396
+-0.1
90.1
1.2930
0.17001
+-0.1
90.1
1.3407
0.22053
+-0.1
90.1
1.3814
0.27556
+-0.1
90.1
1.4153
0.32859
+-0.1
90.1
1.3620
0.24604
+-0.1
90.1
1.3951
0.29404
+-0.1
90.1
1.4232
0.34348
+-0.1
90.1
1.4490
0.39170
+-0.1
90.1
1.4721
0.43922
+-0.1
90.1
1.4944
0.48771
+-0.1
90.1
1.5147
0.53597
+-0.1
90.1
1.5333
0.58487
+-0.1
90.1
1.5489
0.62981
+-0.1
90.1
1.5631
0.67564
+-0.1
90.1
1.5752
0.72155
+-0.1
90.1
1.5849
0.76903
+-0.1
90.1
1.5916
0.81658
+-0.1
90.1
1.5956
0.86455
+-0.1
90.1
1.5948
0.91231
+-0.1
90.1
1.5916
0.95921
+-0.1
90.1
1.5854
0.99755
+-0.1
Isothermal P-T-X Data : ETHANOL + WATER at 108.2C
Reference
KOLBE,B. and J.GMEHLING, Fluid Phase Equilib., 23, 213 (1985)
Method
STATIC METHOD
Number of Data Points = 29
T,deg.C
P,bar
X
Y
T Err
P Err
X Err
Y Err
108.2
1.5332
0.01269
+-0.1
108.2
1.6890
0.02499
+-0.1
108.2
1.9348
0.05136
+-0.1
108.2
2.0864
0.07390
+-0.1
108.2
2.2076
0.09903
+-0.1
108.2
2.2985
0.12425
+-0.1
108.2
2.3672
0.14912
+-0.1
108.2
2.4218
0.17340
+-0.1
108.2
2.4697
0.19843
+-0.1
108.2
2.5114
0.22372
+-0.1
108.2
2.5488
0.24947
+-0.1
108.2
2.5828
0.27460
+-0.1
108.2
2.6093
0.29572
+-0.1
108.2
2.6146
0.29963
+-0.1
108.2
2.6691
0.34909
+-0.1
108.2
2.7186
0.39929
+-0.1
108.2
2.7598
0.44411
+-0.1
108.2
2.8039
0.49674
+-0.1
108.2
2.8421
0.54597
+-0.1
108.2
2.8761
0.59357
+-0.1
108.2
2.9104
0.64923
+-0.1
108.2
2.9360
0.69944
+-0.1
108.2
2.9564
0.74811
+-0.1
108.2
2.9718
0.79934
+-0.1
108.2
2.9808
0.85240
+-0.1
108.2
2.9816
0.89534
+-0.1
108.2
2.9758
0.94316
+-0.1
108.2
2.9663
0.98044
+-0.1
108.2
2.9597
0.99756
+-0.1
Isothermal P-T-X Data : ETHANOL + WATER at 130.3C
Reference
KOLBE,B. and J.GMEHLING, Fluid Phase Equilib., 23, 213 (1985)
Method
STATIC METHOD
Number of Data Points = 30
T,deg.C
P,bar
X
Y
T Err
P Err
X Err
Y Err
130.3
2.9679
0.00820
+-0.1
130.3
3.2267
0.01827
+-0.1
130.3
3.6552
0.03953
+-0.1
130.3
3.8185
0.05007
+-0.1
130.3
4.0152
0.06550
+-0.1
130.3
4.1138
0.07444
+-0.1
130.3
4.3251
0.09795
+-0.1
130.3
4.4623
0.11776
+-0.1
130.3
4.5764
0.13769
+-0.1
130.3
4.6689
0.15673
+-0.1
130.3
4.7442
0.17471
+-0.1
130.3
4.8650
0.20862
+-0.1
130.3
4.9844
0.24866
+-0.1
130.3
5.0867
0.28851
+-0.1
130.3
5.0990
0.29553
+-0.1
130.3
5.2157
0.34797
+-0.1
130.3
5.3046
0.39214
+-0.1
130.3
5.3872
0.43622
+-0.1
130.3
5.4785
0.48912
+-0.1
130.3
5.5561
0.53998
+-0.1
130.3
5.6209
0.58560
+-0.1
130.3
5.6866
0.63966
+-0.1
130.3
5.7390
0.69011
+-0.1
130.3
5.7788
0.73563
+-0.1
130.3
5.8120
0.78834
+-0.1
130.3
5.8311
0.85036
+-0.1
130.3
5.8323
0.88909
+-0.1
130.3
5.8233
0.92932
+-0.1
130.3
5.8040
0.97057
+-0.1
130.3
5.7854
0.99751
+-0.1
Isobaric P-T-X-Y Data : ETHANOL + WATER at 760mmHg
Reference
DALAGER,P., J.Chem.Eng.Data, 14, 298 (1969)
Method
THE METHOD IS BASED ON RADIOACTIVE TRACERS
Number of Data Points = 27
T,deg.C
P,mmHg
X
Y
T Err
P Err
X Err
Y Err
100.00
760
0.000002
0.000034
+-0.02
+-1
100.00
760
0.000002
0.000024
+-0.02
+-1
100.00
760
0.000022
0.000308
+-0.02
+-1
100.00
760
0.000014
0.000280
+-0.02
+-1
100.00
760
0.000014
0.000183
+-0.02
+-1
100.00
760
0.000208
0.002454
+-0.02
+-1
100.00
760
0.000148
0.001591
+-0.02
+-1
100.00
760
0.000187
0.002475
+-0.02
+-1
100.00
760
0.000150
0.001957
+-0.02
+-1
98.50
760
0.004815
0.072680
+-0.02
+-1
98.60
760
0.004014
0.059219
+-0.02
+-1
98.55
760
0.004307
0.059815
+-0.02
+-1
93.00
760
0.0315
0.2582
+-0.02
+-1
92.95
760
0.0370
0.3625
+-0.02
+-1
87.95
760
0.0740
0.3881
+-0.02
+-1
85.10
760
0.1218
0.4658
+-0.02
+-1
84.85
760
0.1283
0.4878
+-0.02
+-1
81.85
760
0.2548
0.5626
+-0.02
+-1
81.90
760
0.2597
0.5539
+-0.02
+-1
80.50
760
0.3937
0.6201
+-0.02
+-1
80.35
760
0.3971
0.6128
+-0.02
+-1
79.30
760
0.5472
0.6789
+-0.02
+-1
78.50
760
0.6980
0.7568
+-0.02
+-1
78.20
760
0.8400
0.8416
+-0.02
+-1
78.20
760
0.8393
0.8391
+-0.02
+-1
78.20
760
0.9140
0.9223
+-0.02
+-1
78.20
760
0.9099
0.9189
+-0.02
+-1
Isothermal P-T-X-Y Data : ETHANOL + WATER at 363.15K
Reference
Pemberton,R.C. and C.J.Mash, J.Chem.Thermodyn., 10, 867 (1978)
Method
Number of Data Points = 24
T,K
P,kPa
X
Y
T Err
P Err
X Err
Y Err
363.15
73.726
0.00429
0.0520
363.15
81.909
0.01507
0.1539
363.15
89.620
0.02693
0.2337
363.15
99.667
0.04594
0.3200
363.15
108.298
0.06731
0.3823
363.15
119.548
0.10939
0.4530
363.15
128.811
0.17057
0.5058
363.15
135.640
0.24642
0.5449
363.15
140.677
0.32356
0.5763
363.15
144.188
0.38800
0.6010
363.15
145.622
0.41705
0.6123
363.15
149.595
0.50445
0.6480
363.15
152.616
0.58044
0.6830
363.15
154.470
0.63399
0.7106
363.15
157.003
0.72433
0.7639
363.15
157.811
0.76364
0.7901
363.15
158.489
0.80833
0.8224
363.15
158.914
0.85783
0.8618
363.15
158.987
0.89065
0.8903
363.15
158.963
0.89935
0.8981
363.15
158.868
0.92445
0.9216
363.15
158.600
0.95370
0.9506
363.15
158.354
0.97315
0.9708
363.15
158.227
0.98153
0.9797
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