2
0
2009
che
xia
0
journal
Original
Chen, S.-n.[Su-ning]
Xia, Q.[Qing]
Lu, L.-f.[Li-fei]
Li, D.[Dong]
Zhang, F.-B.[Feng-Bao]
Zhang, G.-L.[Guo-Liang]
J. Chem. Eng. Data
2009
2020-09-29
Solubility of Sebacic Acid in Binary Mixtures Containing Alcohols
The solubilities of sebacic acid in mixed solvents n-propanol + water have been measured by a dynamic method using a laser monitoring observation technique over a temperature range (288 to 351) K. A synergistic effect on solubility was found to occur in sebacic acid + n-propanol + water mixed systems. To detect the synergistic effect, solubilities of sebacic acid in 14.35 %, 36.97 %, 79.81 %, and 90.00 % mole fraction ethanol aqueous solution were determined to supplement our previous report. A weak synergistic effect was found for sebacic acid + ethanol + water mixed systems. The solid-liquid equilibrium (SLE) data have been fitted using the eh equation, the Wilson equation, and the NRTL equation. The comparison between the experimental and the calculated solubilities for the three models is reasonable, and the root-meansquare deviations for each system range from (0.30 to 1.95) K.
10.1021/je800549f
3
54
776-780
1
InChI=1S/C10H18O4/c11-9(12)7-5-3-1-2-4-6-8-10(13)14/h1-8H2,(H,11,12)(H,13,14)
CXMXRPHRNRROMY-UHFFFAOYSA-N
1,10-decanedioic acid
decanedioic acid
n-decanedioic acid
sebacic acid
C10H18O4
1
Commercial source
1
Crystallization from solution
Dried by oven heating
Crystallization from solution
Dried by oven heating
2
99.4
3
HPLC
2
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
ethanol
ethyl alcohol
C2H6O
1
Commercial source
1
99.7
3
Stated by supplier
2
None used
3
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
BDERNNFJNOPAEC-UHFFFAOYSA-N
propan-1-ol
1-propanol
n-propanol
n-propyl alcohol
C3H8O
1
Commercial source
1
99.8
3
Stated by supplier
2
None used
4
InChI=1S/H2O/h1H2
XLYOFNOQVPJJNP-UHFFFAOYSA-N
water
H2O
1
Commercial source
1
99.5
3
Estimated by the compiler
1
3
1
1
1
Principal objective of the work
RDC
TRC
4/29/2009
1
Solid-liquid equilibrium temperature, K
laser monitoring
Liquid
Direct value, X
3
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Crystal
1
1
Pressure, kPa
Liquid
101.3
2
1
Mole fraction
1
Liquid
1
0.009
4
1
292
5
1
1
1
0.01353
4
1
297.66
5
1
1
1
0.01624
4
1
300.34
5
1
1
1
0.02127
4
1
304.99
5
1
1
1
0.02606
4
1
308.87
5
1
1
1
0.03004
4
1
311.8
5
1
1
1
0.03442
4
1
314.56
5
1
1
1
0.04289
4
1
318.74
5
1
1
1
0.04756
4
1
321.5
5
1
1
1
0.05294
4
1
323.44
5
1
1
1
0.06141
4
1
327.14
5
1
1
1
0.07582
4
1
331.86
5
1
1
1
0.09025
4
1
336.76
5
1
1
1
0.09561
4
1
337.71
5
1
1
1
0.1086
4
1
340.3
5
1
1
1
0.1096
4
1
340.35
5
1
1
1
0.118
4
1
342.05
5
1
1
1
0.1333
4
1
345.08
5
1
1
1
0.1425
4
1
347.47
5
1
1
1
0.1548
4
1
348.62
5
1
1
2
3
1
1
1
4
1
Principal objective of the work
RDC
TRC
4/29/2009
1
Solid-liquid equilibrium temperature, K
laser monitoring
Liquid
Direct value, X
3
4
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Crystal
1
1
Pressure, kPa
Liquid
101
3
1
Solvent: Mole fraction
3
Liquid
2
Mole fraction
1
Liquid
1
0.2
4
2
0.00275
4
1
295.41
5
1
1
1
0.2
4
2
0.00295
4
1
296.72
5
1
1
1
0.2
4
2
0.00475
4
1
300.83
5
1
1
1
0.2
4
2
0.00604
4
1
303.93
5
1
1
1
0.2
4
2
0.00663
4
1
305.74
5
1
1
1
0.2
4
2
0.00858
4
1
309.56
5
1
1
1
0.2
4
2
0.00945
4
1
311.1
5
1
1
1
0.2
4
2
0.01084
4
1
313.47
5
1
1
1
0.2
4
2
0.01229
4
1
315.38
5
1
1
1
0.2
4
2
0.01431
4
1
317.73
5
1
1
1
0.2
4
2
0.01789
4
1
322.99
5
1
1
1
0.2
4
2
0.01968
4
1
324.89
5
1
1
1
0.2
4
2
0.0258
4
1
329.28
5
1
1
1
0.2
4
2
0.0316
4
1
332.94
5
1
1
1
0.2
4
2
0.03927
4
1
335.8
5
1
1
1
0.2
4
2
0.04446
4
1
338.32
5
1
1
1
0.2
4
2
0.05075
4
1
340.5
5
1
1
1
0.4
4
2
0.00506
4
1
291.32
5
1
1
1
0.4
4
2
0.00912
4
1
294
5
1
1
1
0.4
4
2
0.00947
4
1
295.65
5
1
1
1
0.4
4
2
0.01014
4
1
295.95
5
1
1
1
0.4
4
2
0.01235
4
1
299.97
5
1
1
1
0.4
4
2
0.01488
4
1
302.24
5
1
1
1
0.4
4
2
0.01879
4
1
307.14
5
1
1
1
0.4
4
2
0.02151
4
1
309.32
5
1
1
1
0.4
4
2
0.02593
4
1
312.9
5
1
1
1
0.4
4
2
0.03018
4
1
316.1
5
1
1
1
0.4
4
2
0.0342
4
1
318.34
5
1
1
1
0.4
4
2
0.03838
4
1
321.05
5
1
1
1
0.4
4
2
0.04275
4
1
323.37
5
1
1
1
0.4
4
2
0.04951
4
1
326.35
5
1
1
1
0.4
4
2
0.0559
4
1
328.52
5
1
1
1
0.4
4
2
0.06435
4
1
332.32
5
1
1
1
0.4
4
2
0.07124
4
1
334.72
5
1
1
1
0.4
4
2
0.0784
4
1
336.74
5
1
1
1
0.4
4
2
0.08466
4
1
338.24
5
1
1
1
0.4
4
2
0.09326
4
1
340.76
5
1
1
1
0.4
4
2
0.1023
4
1
342.77
5
1
1
1
0.4
4
2
0.1123
4
1
345.12
5
1
1
1
0.4
4
2
0.1235
4
1
347.84
5
1
1
1
0.4
4
2
0.1334
4
1
349.77
5
1
1
1
0.6011
4
2
0.00967
4
1
292.05
5
1
1
1
0.6011
4
2
0.01402
4
1
295.65
5
1
1
1
0.6011
4
2
0.01746
4
1
298.75
5
1
1
1
0.6011
4
2
0.02319
4
1
302.96
5
1
1
1
0.6011
4
2
0.02851
4
1
307.59
5
1
1
1
0.6011
4
2
0.03288
4
1
311.08
5
1
1
1
0.6011
4
2
0.03714
4
1
314.44
5
1
1
1
0.6011
4
2
0.04364
4
1
316.82
5
1
1
1
0.6011
4
2
0.05089
4
1
320.6
5
1
1
1
0.6011
4
2
0.05655
4
1
322.35
5
1
1
1
0.6011
4
2
0.06181
4
1
325.15
5
1
1
1
0.6011
4
2
0.06739
4
1
327.45
5
1
1
1
0.6011
4
2
0.07662
4
1
331.15
5
1
1
1
0.6011
4
2
0.08673
4
1
334.8
5
1
1
1
0.6011
4
2
0.09363
4
1
336.71
5
1
1
1
0.6011
4
2
0.1055
4
1
338.5
5
1
1
1
0.6011
4
2
0.1171
4
1
341.32
5
1
1
1
0.6011
4
2
0.1294
4
1
344.31
5
1
1
1
0.6011
4
2
0.1427
4
1
347.66
5
1
1
1
0.8003
4
2
0.01355
4
1
292.21
5
1
1
1
0.8003
4
2
0.01786
4
1
297.06
5
1
1
1
0.8003
4
2
0.02346
4
1
301.92
5
1
1
1
0.8003
4
2
0.02847
4
1
305.97
5
1
1
1
0.8003
4
2
0.03279
4
1
309.37
5
1
1
1
0.8003
4
2
0.03623
4
1
311.66
5
1
1
1
0.8003
4
2
0.04338
4
1
316.25
5
1
1
1
0.8003
4
2
0.04846
4
1
318.03
5
1
1
1
0.8003
4
2
0.05555
4
1
321.3
5
1
1
1
0.8003
4
2
0.06137
4
1
324
5
1
1
1
0.8003
4
2
0.06812
4
1
327.07
5
1
1
1
0.8003
4
2
0.08864
4
1
333.29
5
1
1
1
0.8003
4
2
0.09676
4
1
335.43
5
1
1
1
0.8003
4
2
0.1092
4
1
339.05
5
1
1
1
0.8003
4
2
0.1221
4
1
342.15
5
1
1
1
0.8003
4
2
0.1354
4
1
345
5
1
1
1
1
4
2
0.009
4
1
292
5
1
1
1
1
4
2
0.01353
4
1
297.66
5
1
1
1
1
4
2
0.01624
4
1
300.34
5
1
1
1
1
4
2
0.02127
4
1
304.99
5
1
1
1
1
4
2
0.02606
4
1
308.87
5
1
1
1
1
4
2
0.03004
4
1
311.8
5
1
1
1
1
4
2
0.03442
4
1
314.56
5
1
1
1
1
4
2
0.04289
4
1
318.74
5
1
1
1
1
4
2
0.04756
4
1
321.5
5
1
1
1
1
4
2
0.05294
4
1
323.44
5
1
1
1
1
4
2
0.06141
4
1
327.14
5
1
1
1
1
4
2
0.07582
4
1
331.86
5
1
1
1
1
4
2
0.09025
4
1
336.76
5
1
1
1
1
4
2
0.09561
4
1
337.71
5
1
1
1
1
4
2
0.1086
4
1
340.3
5
1
1
1
1
4
2
0.1096
4
1
340.35
5
1
1
1
1
4
2
0.118
4
1
342.05
5
1
1
1
1
4
2
0.1333
4
1
345.08
5
1
1
1
1
4
2
0.1425
4
1
347.47
5
1
1
1
1
4
2
0.1548
4
1
348.62
5
1
1
3
2
1
1
1
4
1
Principal objective of the work
RDC
TRC
4/29/2009
1
Solid-liquid equilibrium temperature, K
laser monitoring
Liquid
Direct value, X
2
4
1
Data file compiler
Propagation of evaluated standard uncertainties
95
Liquid
Crystal
1
1
Pressure, kPa
Liquid
101
3
1
Solvent: Mole fraction
2
Liquid
2
Mole fraction
1
Liquid
1
0.1435
4
2
6.041e-05
4
1
289.3
5
1
1
1
0.1435
4
2
9.592e-05
4
1
295.54
5
1
1
1
0.1435
4
2
0.0001164
4
1
295.59
5
1
1
1
0.1435
4
2
0.0002297
4
1
303.14
5
1
1
1
0.1435
4
2
0.0003659
4
1
305.49
5
1
1
1
0.1435
4
2
0.0004959
4
1
308.31
5
1
1
1
0.1435
4
2
0.0006598
4
1
310.34
5
1
1
1
0.1435
4
2
0.000857
4
1
313.16
5
1
1
1
0.1435
4
2
0.00112
4
1
317.05
5
1
1
1
0.1435
4
2
0.001432
4
1
319.8
5
1
1
1
0.1435
4
2
0.001862
4
1
322.49
5
1
1
1
0.1435
4
2
0.002552
4
1
325.53
5
1
1
1
0.1435
4
2
0.003304
4
1
327.71
5
1
1
1
0.1435
4
2
0.005117
4
1
330.68
5
1
1
1
0.1435
4
2
0.007287
4
1
334.78
5
1
1
1
0.1435
4
2
0.01039
4
1
337.59
5
1
1
1
0.1435
4
2
0.01431
4
1
340.74
5
1
1
1
0.1435
4
2
0.0179
4
1
343.69
5
1
1
1
0.1435
4
2
0.02065
4
1
345.8
5
1
1
1
0.1435
4
2
0.02572
4
1
348.68
5
1
1
1
0.1435
4
2
0.02892
4
1
350.74
5
1
1
1
0.3697
4
2
0.0009859
4
1
288.47
5
1
1
1
0.3697
4
2
0.001752
4
1
290.55
5
1
1
1
0.3697
4
2
0.002669
4
1
292.67
5
1
1
1
0.3697
4
2
0.003383
4
1
296.97
5
1
1
1
0.3697
4
2
0.004199
4
1
298.05
5
1
1
1
0.3697
4
2
0.005313
4
1
300.16
5
1
1
1
0.3697
4
2
0.00679
4
1
303.65
5
1
1
1
0.3697
4
2
0.008567
4
1
306.66
5
1
1
1
0.3697
4
2
0.009566
4
1
309.06
5
1
1
1
0.3697
4
2
0.01131
4
1
309.87
5
1
1
1
0.3697
4
2
0.01445
4
1
313.7
5
1
1
1
0.3697
4
2
0.01567
4
1
316.14
5
1
1
1
0.3697
4
2
0.01975
4
1
318.45
5
1
1
1
0.3697
4
2
0.02411
4
1
321.57
5
1
1
1
0.3697
4
2
0.02939
4
1
325.86
5
1
1
1
0.3697
4
2
0.03071
4
1
326.92
5
1
1
1
0.3697
4
2
0.03621
4
1
328.87
5
1
1
1
0.3697
4
2
0.04242
4
1
331.34
5
1
1
1
0.3697
4
2
0.04908
4
1
334.33
5
1
1
1
0.3697
4
2
0.05562
4
1
336.44
5
1
1
1
0.3697
4
2
0.06235
4
1
338.74
5
1
1
1
0.3697
4
2
0.06906
4
1
340.33
5
1
1
1
0.3697
4
2
0.07357
4
1
341.96
5
1
1
1
0.3697
4
2
0.08348
4
1
344.16
5
1
1
1
0.3697
4
2
0.09221
4
1
346.04
5
1
1
1
0.3697
4
2
0.1002
4
1
348.01
5
1
1
1
0.3697
4
2
0.1085
4
1
350.08
5
1
1
1
0.7981
4
2
0.0094
4
1
292.46
5
1
1
1
0.7981
4
2
0.01451
4
1
295.74
5
1
1
1
0.7981
4
2
0.02024
4
1
300.8
5
1
1
1
0.7981
4
2
0.02476
4
1
305.24
5
1
1
1
0.7981
4
2
0.02975
4
1
308.56
5
1
1
1
0.7981
4
2
0.03533
4
1
311.91
5
1
1
1
0.7981
4
2
0.04198
4
1
316.01
5
1
1
1
0.7981
4
2
0.05025
4
1
319.91
5
1
1
1
0.7981
4
2
0.05489
4
1
321.52
5
1
1
1
0.7981
4
2
0.06388
4
1
325.39
5
1
1
1
0.7981
4
2
0.07326
4
1
328.73
5
1
1
1
0.7981
4
2
0.08456
4
1
332.44
5
1
1
1
0.7981
4
2
0.09393
4
1
335.53
5
1
1
1
0.7981
4
2
0.1046
4
1
337.88
5
1
1
1
0.7981
4
2
0.1167
4
1
340.48
5
1
1
1
0.7981
4
2
0.1306
4
1
344.04
5
1
1
1
0.9
4
2
0.02702
4
1
305.77
5
1
1
1
0.9
4
2
0.03892
4
1
313.76
5
1
1
1
0.9
4
2
0.05358
4
1
321.26
5
1
1