Contents
Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[322.22; 384.50]
J/mol×K
[535.02; 718.73]
Cp,gas
322.22
J/mol×K
535.02
Joback Calculated Property
Cp,gas
333.68
J/mol×K
565.64
Joback Calculated Property
Cp,gas
344.72
J/mol×K
596.26
Joback Calculated Property
Cp,gas
355.33
J/mol×K
626.88
Joback Calculated Property
Cp,gas
365.50
J/mol×K
657.50
Joback Calculated Property
Cp,gas
375.23
J/mol×K
688.12
Joback Calculated Property
Cp,gas
384.50
J/mol×K
718.73
Joback Calculated Property
Cp,liquid
[330.50; 338.10]
J/mol×K
[292.60; 298.15]
Cp,liquid
338.10
J/mol×K
292.60
NIST
Cp,liquid
338.10
J/mol×K
292.60
NIST
Cp,liquid
330.50
J/mol×K
298.15
NIST
η
[0.0002287; 0.0020386]
Pa×s
[324.24; 535.02]
η
0.0020386
Pa×s
324.24
Joback Calculated Property
η
0.0011847
Pa×s
359.37
Joback Calculated Property
η
0.0007583
Pa×s
394.50
Joback Calculated Property
η
0.0005222
Pa×s
429.63
Joback Calculated Property
η
0.0003804
Pa×s
464.76
Joback Calculated Property
η
0.0002898
Pa×s
499.89
Joback Calculated Property
η
0.0002287
Pa×s
535.02
Joback Calculated Property
Δvap H
56.50
kJ/mol
408.50
NIST
Pvap
[4.95e-03; 0.34]
kPa
[290.20; 345.50]
Pvap
4.95e-03
kPa
290.20
Vapor P...
Pvap
5.04e-03
kPa
290.50
Vapor P...
Pvap
6.78e-03
kPa
293.50
Vapor P...
Pvap
8.61e-03
kPa
296.40
Vapor P...
Pvap
0.01
kPa
301.40
Vapor P...
Pvap
0.02
kPa
306.40
Vapor P...
Pvap
0.03
kPa
311.40
Vapor P...
Pvap
0.04
kPa
313.40
Vapor P...
Pvap
0.05
kPa
316.40
Vapor P...
Pvap
0.05
kPa
318.40
Vapor P...
Pvap
0.07
kPa
321.40
Vapor P...
Pvap
0.08
kPa
323.50
Vapor P...
Pvap
0.09
kPa
326.50
Vapor P...
Pvap
0.10
kPa
326.50
Vapor P...
Pvap
0.11
kPa
328.50
Vapor P...
Pvap
0.13
kPa
331.40
Vapor P...
Pvap
0.14
kPa
331.60
Vapor P...
Pvap
0.15
kPa
333.60
Vapor P...
Pvap
0.19
kPa
336.50
Vapor P...
Pvap
0.22
kPa
339.40
Vapor P...
Pvap
0.27
kPa
342.40
Vapor P...
Pvap
0.34
kPa
345.50
Vapor P...
ρl
[966.91; 1044.83]
kg/m3
[288.15; 363.15]
ρl
1044.83
kg/m3
288.15
Volumet...
ρl
1039.63
kg/m3
293.15
Volumet...
ρl
1034.44
kg/m3
298.15
Volumet...
ρl
1035.34
kg/m3
298.20
Modelin...
ρl
1029.25
kg/m3
303.15
Volumet...
ρl
1029.59
kg/m3
303.15
Surface...
ρl
1024.40
kg/m3
308.15
Surface...
ρl
1024.08
kg/m3
308.15
Volumet...
ρl
1018.90
kg/m3
313.15
Volumet...
ρl
1019.20
kg/m3
313.15
Surface...
ρl
1014.01
kg/m3
318.15
Surface...
ρl
1013.72
kg/m3
318.15
Volumet...
ρl
1008.81
kg/m3
323.15
Surface...
ρl
1008.55
kg/m3
323.15
Volumet...
ρl
1003.60
kg/m3
328.15
Surface...
ρl
998.39
kg/m3
333.15
Surface...
ρl
993.16
kg/m3
338.15
Surface...
ρl
987.93
kg/m3
343.15
Surface...
ρl
982.70
kg/m3
348.15
Surface...
ρl
977.45
kg/m3
353.15
Surface...
ρl
972.19
kg/m3
358.15
Surface...
ρl
966.91
kg/m3
363.15
Surface...
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
378.20
K
2.00
NIST
Datasets
Mass density, kg/m3 (1)
Thermal conductivity, W/m/K (1)
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.57
100.00
1049.61
283.57
1000.00
1050.21
283.57
3000.00
1051.56
283.57
5000.00
1052.88
283.57
10000.00
1056.11
283.57
15000.00
1059.25
283.58
20000.00
1062.29
283.58
25000.00
1065.25
283.57
30000.00
1068.16
283.57
40000.00
1073.71
283.57
50000.00
1079.0
283.57
60000.00
1084.1
283.57
70000.00
1089.01
283.57
80000.00
1093.63
283.57
90010.00
1098.12
283.56
100010.00
1102.48
293.49
100.00
1039.78
293.50
1000.00
1040.41
293.50
3000.00
1041.81
293.50
5000.00
1043.2
293.50
10000.00
1046.6
293.50
15000.00
1049.91
293.49
20000.00
1053.11
293.49
25000.00
1056.23
293.50
30000.00
1059.25
293.49
40000.00
1065.07
293.50
50000.00
1070.61
293.49
60000.00
1075.9
293.50
70000.00
1080.89
293.50
80000.00
1085.77
293.51
90000.00
1090.39
293.51
100000.00
1094.9
303.42
100.00
1028.98
303.42
1000.00
1029.62
303.43
3000.00
1031.12
303.43
5000.00
1032.59
303.44
10000.00
1036.15
303.43
15000.00
1039.61
303.42
20000.00
1042.98
303.42
25000.00
1046.26
303.43
30000.00
1049.4
303.43
40000.00
1055.5
303.43
50000.00
1061.26
303.42
60000.00
1066.78
303.42
70000.00
1072.05
303.42
80000.00
1077.09
303.43
90000.00
1081.92
303.43
100000.00
1086.58
313.33
100.00
1018.75
313.33
1000.00
1019.44
313.33
3000.00
1021.07
313.32
5000.00
1022.61
313.32
10000.00
1026.44
313.31
15000.00
1030.05
313.33
20000.00
1033.63
313.33
25000.00
1037.06
313.32
30000.00
1040.39
313.32
40000.00
1046.78
313.31
50000.00
1052.81
313.33
60000.00
1058.52
313.33
70000.00
1064.01
313.33
80000.00
1069.21
313.33
90000.00
1074.2
313.33
100000.00
1078.99
323.18
100.00
1008.44
323.18
1000.00
1009.19
323.18
3000.00
1010.86
323.19
5000.00
1012.5
323.18
10000.00
1016.52
323.18
15000.00
1020.37
323.18
20000.00
1024.08
323.18
25000.00
1027.7
323.19
30000.00
1031.17
323.19
40000.00
1037.8
323.19
50000.00
1044.06
323.19
60000.00
1050.01
323.19
70000.00
1055.67
323.19
80000.00
1061.06
323.19
90000.00
1066.22
323.19
100000.00
1071.19
333.10
100.00
998.31
333.10
1000.00
999.11
333.10
3000.00
1000.91
333.10
5000.00
1002.64
333.11
10000.00
1006.85
333.11
15000.00
1010.94
333.11
20000.00
1014.85
333.11
25000.00
1018.62
333.11
30000.00
1022.27
333.11
40000.00
1029.2
333.11
50000.00
1035.72
333.11
60000.00
1041.91
333.11
70000.00
1047.69
333.11
80000.00
1053.26
333.11
90000.00
1058.57
333.11
100000.00
1063.7
342.97
100.00
987.87
342.98
1000.00
988.73
342.98
3000.00
990.63
342.98
5000.00
992.45
342.98
10000.00
996.91
342.97
15000.00
1001.22
342.97
20000.00
1005.3
342.98
25000.00
1009.24
342.97
30000.00
1013.07
342.97
40000.00
1020.32
342.97
50000.00
1027.1
342.98
60000.00
1033.53
342.97
70000.00
1039.64
342.98
80000.00
1045.43
342.97
90000.00
1050.91
342.97
100000.00
1056.19
352.82
100.00
977.64
352.82
1000.00
978.58
352.82
3000.00
980.59
352.82
5000.00
982.53
352.82
10000.00
987.26
352.82
15000.00
991.79
352.83
20000.00
996.08
352.83
25000.00
1000.24
352.83
30000.00
1004.25
352.83
40000.00
1011.8
352.83
50000.00
1018.87
352.83
60000.00
1025.54
352.83
70000.00
1031.82
352.83
80000.00
1037.81
352.83
90000.00
1043.47
352.83
100010.00
1048.95
362.66
100.00
967.3
362.66
1000.00
968.28
362.66
3000.00
970.41
362.67
5000.00
972.48
362.67
10000.00
977.45
362.67
15000.00
982.21
362.67
20000.00
986.74
362.67
25000.00
991.07
362.67
30000.00
995.26
362.67
40000.00
1003.16
362.67
50000.00
1010.5
362.66
60000.00
1017.41
362.67
70000.00
1023.98
362.67
80000.00
1030.14
362.67
90000.00
1036.01
362.67
100000.00
1041.65
Reference
Thermal conductivity, W/m/K
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Thermal conductivity, W/m/K - Liquid
264.81
5000.00
0.1565
265.06
100.00
0.1559
265.23
15000.00
0.1602
265.57
15000.00
0.1596
265.83
10000.00
0.1586
265.83
20000.00
0.1615
265.94
20000.00
0.1602
266.08
15000.00
0.1594
266.13
10000.00
0.1582
266.38
100.00
0.1561
266.47
5000.00
0.1571
266.81
20000.00
0.1607
266.94
5000.00
0.1572
267.04
100.00
0.1561
267.83
10000.00
0.1589
284.87
20000.00
0.1580
285.16
10000.00
0.1556
285.41
20000.00
0.1579
285.62
5000.00
0.1539
285.63
100.00
0.1527
285.68
15000.00
0.1570
285.71
10000.00
0.1554
286.14
5000.00
0.1537
286.27
15000.00
0.1569
286.33
100.00
0.1528
286.36
10000.00
0.1555
286.56
15000.00
0.1562
286.61
5000.00
0.1538
286.76
20000.00
0.1578
287.36
15000.00
0.1563
287.43
5000.00
0.1535
287.75
100.00
0.1527
304.47
100.00
0.1484
304.53
15000.00
0.1529
304.85
20000.00
0.1551
305.64
20000.00
0.1543
305.66
100.00
0.1483
305.72
10000.00
0.1518
306.12
5000.00
0.1497
306.12
15000.00
0.1529
306.39
20000.00
0.1549
306.44
10000.00
0.1519
306.79
5000.00
0.1501
306.80
15000.00
0.1529
306.84
10000.00
0.1513
307.27
10000.00
0.1510
307.29
5000.00
0.1502
307.33
100.00
0.1482
326.02
100.00
0.1436
326.76
100.00
0.1433
327.17
10000.00
0.1466
327.21
5000.00
0.1448
327.56
100.00
0.1437
327.58
15000.00
0.1489
327.69
20000.00
0.1503
327.81
5000.00
0.1449
328.07
10000.00
0.1471
328.35
15000.00
0.1484
328.56
20000.00
0.1502
328.57
5000.00
0.1449
328.62
10000.00
0.1469
329.63
5000.00
0.1453
329.69
15000.00
0.1481
330.11
20000.00
0.1501
345.18
20000.00
0.1462
345.49
5000.00
0.1404
345.53
100.00
0.1385
345.80
10000.00
0.1422
345.99
5000.00
0.1402
346.11
5000.00
0.1404
346.18
15000.00
0.1448
346.44
10000.00
0.1423
346.52
15000.00
0.1442
346.59
20000.00
0.1462
346.63
100.00
0.1384
346.65
15000.00
0.1446
346.94
20000.00
0.1461
347.16
100.00
0.1385
347.34
10000.00
0.1419
365.09
100.00
0.1339
365.15
10000.00
0.1381
365.16
5000.00
0.1359
365.54
15000.00
0.1395
365.59
5000.00
0.1360
365.79
100.00
0.1341
366.05
20000.00
0.1409
366.11
10000.00
0.1380
366.50
100.00
0.1339
366.54
20000.00
0.1409
366.57
15000.00
0.1399
366.66
20000.00
0.1415
366.72
10000.00
0.1379
367.17
5000.00
0.1358
367.25
20000.00
0.1415
367.31
15000.00
0.1397
385.28
20000.00
0.1379
385.51
10000.00
0.1325
385.95
10000.00
0.1326
385.95
15000.00
0.1349
385.96
20000.00
0.1384
386.02
5000.00
0.1309
386.08
100.00
0.1284
386.15
5000.00
0.1301
386.36
100.00
0.1279
386.50
15000.00
0.1349
386.63
20000.00
0.1378
386.70
5000.00
0.1304
386.80
10000.00
0.1327
386.93
10000.00
0.1321
386.95
5000.00
0.1303
387.06
15000.00
0.1352
387.25
100.00
0.1278
Reference
Correlations
Similar Compounds
Find more compounds similar to Butanedioic acid, diethyl ester .
Mixtures
Butanoic acid + Butanedioic acid, diethyl ester + Water
Formic acid + Butanedioic acid, diethyl ester + Water
Butanedioic acid, diethyl ester + Water
Butanedioic acid, diethyl ester + Propanoic acid + Water
1-Propanol + Butanedioic acid, diethyl ester
1-Butanol + Butanedioic acid, diethyl ester
Butanedioic acid, diethyl ester + 1-Hexanol
1-Propanol, 2-methyl- + Butanedioic acid, diethyl ester
1-Butanol, 3-methyl- + Butanedioic acid, diethyl ester
Acetonitrile + Butanedioic acid, diethyl ester
Acetic acid + Butanedioic acid, diethyl ester + Water
Carbon dioxide + Butanedioic acid, diethyl ester
Carbon dioxide + Ethanol + Butanedioic acid, diethyl ester
Carbon dioxide + Butanedioic acid, diethyl ester + Ethyl Acetate
Butanoic acid, ethyl ester + Butanedioic acid, diethyl ester
Butanoic acid, ethyl ester + 1-Propanol, 2-methyl- + Butanedioic acid, diethyl ester
Butanedioic acid, diethyl ester + Ethyl Acetate
Acetic acid + Butanedioic acid, diethyl ester
Butanedioic acid, diethyl ester + Ethyl Acetate + Water
Ethanol + Butanedioic acid, diethyl ester
Find more mixtures with Butanedioic acid, diethyl ester .
Sources
KDB Vapor Pressure Data
Crippen Method
Phase equilibria for reactive distillation of diethyl succinate. Part II: Systems diethyl succinate + ethyl acetate + water and diethyl succinate + acetic acid + water
Phase equilibria for reactive distillation of diethyl succinate Part I. System diethyl succinate + ethanol + water
Liquid-liquid equilibria of (water + butyric acid + diethyl succinate or diethyl glutarate or diethyl adipate) ternary systems
Critical temperatures and pressures of some dicarboxylic acid diethyl esters
Modeling phase equilibria of ternary systems (water + formic acid + ester or alcohol) through UNIFAC-original, SERLAS, NRTL, NRTL-modified, and three-suffix Margules: Parameter estimation using genetic algorithm
Surface tension of four oxygenated fuels: experiment and correlation
Phase equilibrium measurements and thermodynamic modeling of {CO2 + diethyl succinate + cosolvent} systems
(Liquid + liquid) equilibria of (water + propionic acid + diethyl succinate or diethyl glutarate or diethyl adipate) ternary systems
Volumetric and viscometric study with FT-IR analysis of binary systems with diethyl succinate and alcohols
Volumetric, viscometric, spectral studies and viscosity modelling of binary mixtures of esters and alcohols (diethyl succinate, or ethyl octanoate + isobutanol, or isopentanol) at varying temperatures
Liquid Density of 2 Methoxyethyl Acetate, 2 Ethylhexyl Acetate and Diethyl Succinate at Temperatures from 283.15 K to 363.15 K and Pressures up to 100 MPa
Density, Viscosity, and Refractive Index Data for a Ternary System of Wine Congeners (Ethyl Butyrate + Diethyl Succinate + Isobutanol) in the Temperature Range from 288.15 to 323.15 K and at Atmospheric Pressure
Phase Behavior of Binary Mixtures Containing Succinic Acid or Its Esters
Vapor Pressures and Enthalpies of Vaporization of a Series of the Symmetric Linear n-Alkyl Esters of Dicarboxylic Acids
Phase Equilibrium and Physical Properties for the Purification of Propylene Carbonate (PC) and y-Butyrolactone (GBL)
Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
Thermal Conductivity of Liquid 2-Methoxyethyl Acetate, 2-Ethylhexyl Acetate, and Diethyl Succinate
Vapor Liquid Phase Equilibrium Data of CO2 in Some Physical Solvents from 285.19 K to 313.26 K
Liquid-Liquid Equilibria of (Water + Acetic Acid + Diethyl Succinate or Diethyl Glutarate or Diethyl Adipate) Ternary Systems
Joback Method
KDB
Aqueous Solubility Prediction Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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