Physical Properties
Property
Value
Unit
Source
ω
0.2510
KDB
PAff
754.10
kJ/mol
NIST
Tig
838.15
K
KDB
BasG
725.80
kJ/mol
NIST
Δc H°liquid
-3111.90 ± 0.67
kJ/mol
NIST
μ
1.50
debye
KDB
Tflash,oc
324.26
K
KDB
Δf G°
138.60
kJ/mol
KDB
Δf H°gas
105.10
kJ/mol
KDB
Δf H°liquid
[58.60; 60.90]
kJ/mol
Δf H°liquid
58.60
kJ/mol
NIST
Δf H°liquid
60.90 ± 4.10
kJ/mol
NIST
Δfus H°
10.62
kJ/mol
Joback Calculated Property
Δvap H°
[37.90; 44.80]
kJ/mol
Δvap H°
44.54
kJ/mol
NIST
Δvap H°
44.80
kJ/mol
NIST
Δvap H°
44.50 ± 0.10
kJ/mol
NIST
Δvap H°
44.54 ± 0.04
kJ/mol
NIST
Δvap H°
37.90 ± 0.03
kJ/mol
NIST
IE
[8.95; 9.45]
eV
IE
9.00 ± 0.03
eV
NIST
IE
9.00
eV
NIST
IE
9.00
eV
NIST
IE
9.02
eV
NIST
IE
9.05 ± 0.02
eV
NIST
IE
8.98 ± 0.02
eV
NIST
IE
8.98
eV
NIST
IE
Outlier 9.45
eV
NIST
IE
8.97 ± 0.02
eV
NIST
IE
8.99
eV
NIST
IE
9.03 ± 0.01
eV
NIST
IE
8.98 ± 0.03
eV
NIST
IE
8.95
eV
NIST
IE
8.98 ± 0.02
eV
NIST
IE
8.99
eV
NIST
IE
9.04
eV
NIST
IE
9.05
eV
NIST
IE
8.99 ± 0.03
eV
NIST
IE
9.00
eV
NIST
log 10 WS
[-2.55; -2.55]
log 10 WS
-2.55
Aq. Sol...
log 10 WS
-2.55
Estimat...
log Poct/wat
2.449
Crippen Calculated Property
McVol
89.140
ml/mol
McGowan Calculated Property
NFPA Fire
2
KDB
NFPA Health
2
KDB
Pc
4520.00
kPa
KDB
Inp
[150.00; 983.00]
Inp
960.00
NIST
Inp
952.20
NIST
Inp
931.71
NIST
Inp
941.36
NIST
Inp
924.00
NIST
Inp
932.00
NIST
Inp
914.70
NIST
Inp
923.70
NIST
Inp
934.80
NIST
Inp
959.60
NIST
Inp
961.00
NIST
Inp
974.00
NIST
Inp
974.00
NIST
Inp
964.00
NIST
Inp
964.00
NIST
Inp
945.00
NIST
Inp
925.80
NIST
Inp
965.00
NIST
Inp
982.00
NIST
Inp
979.60
NIST
Inp
941.00
NIST
Inp
903.90
NIST
Inp
926.00
NIST
Inp
909.50
NIST
Inp
919.67
NIST
Inp
921.35
NIST
Inp
926.64
NIST
Inp
927.00
NIST
Inp
927.00
NIST
Inp
918.00
NIST
Inp
915.00
NIST
Inp
930.00
NIST
Inp
921.00
NIST
Inp
935.00
NIST
Inp
982.00
NIST
Inp
936.00
NIST
Inp
895.00
NIST
Inp
983.00
NIST
Inp
910.00
NIST
Inp
936.00
NIST
Inp
945.00
NIST
Inp
930.00
NIST
Inp
945.00
NIST
Inp
Outlier 150.00
NIST
I
[1330.00; 1391.00]
I
1351.00
NIST
I
1338.00
NIST
I
1330.00
NIST
I
1381.03
NIST
I
1373.68
NIST
I
1358.59
NIST
I
1348.92
NIST
I
1391.00
NIST
I
1338.00
NIST
I
1365.00
NIST
S°liquid
[207.90; 21922.00]
J/mol×K
S°liquid
21922.00
J/mol×K
NIST
S°liquid
207.90
J/mol×K
NIST
Tboil
429.21
K
KDB
Tc
670.00
K
KDB
Tfus
[242.25; 242.50]
K
Tfus
242.50
K
KDB
Tfus
242.25
K
Aq. Sol...
Ttriple
[242.40; 242.42]
K
Ttriple
242.40
K
KDB
Ttriple
242.42 ± 0.02
K
NIST
Ttriple
242.40 ± 0.01
K
NIST
Ttriple
242.40 ± 0.20
K
NIST
Vc
0.324
m3 /kmol
KDB
Zc
0.2628890
KDB
Zra
0.26
KDB
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[135.44; 182.34]
J/mol×K
[429.52; 665.41]
Cp,gas
135.44
J/mol×K
429.52
Joback Calculated Property
Cp,gas
144.94
J/mol×K
468.84
Joback Calculated Property
Cp,gas
153.71
J/mol×K
508.15
Joback Calculated Property
Cp,gas
161.79
J/mol×K
547.47
Joback Calculated Property
Cp,gas
169.22
J/mol×K
586.78
Joback Calculated Property
Cp,gas
176.06
J/mol×K
626.10
Joback Calculated Property
Cp,gas
182.34
J/mol×K
665.41
Joback Calculated Property
Cp,liquid
[127.60; 167.15]
J/mol×K
[231.70; 353.15]
Cp,liquid
127.60
J/mol×K
231.70
NIST
Cp,liquid
151.63
J/mol×K
283.15
Heat Ca...
Cp,liquid
151.99
J/mol×K
285.15
Heat Ca...
Cp,liquid
152.37
J/mol×K
287.15
Heat Ca...
Cp,liquid
152.75
J/mol×K
289.15
Heat Ca...
Cp,liquid
153.14
J/mol×K
291.15
Heat Ca...
Cp,liquid
153.54
J/mol×K
293.15
Heat Ca...
Cp,liquid
151.50
J/mol×K
293.20
NIST
Cp,liquid
153.94
J/mol×K
295.15
Heat Ca...
Cp,liquid
154.35
J/mol×K
297.15
Heat Ca...
Cp,liquid
151.00
J/mol×K
298.00
NIST
Cp,liquid
155.39
J/mol×K
298.10
NIST
Cp,liquid
154.29
J/mol×K
298.15
NIST
Cp,liquid
154.77
J/mol×K
299.15
Heat Ca...
Cp,liquid
155.19
J/mol×K
301.15
Heat Ca...
Cp,liquid
145.60
J/mol×K
302.60
NIST
Cp,liquid
145.60
J/mol×K
302.60
NIST
Cp,liquid
155.62
J/mol×K
303.15
Heat Ca...
Cp,liquid
155.90
J/mol×K
303.15
NIST
Cp,liquid
156.05
J/mol×K
305.15
Heat Ca...
Cp,liquid
156.49
J/mol×K
307.15
Heat Ca...
Cp,liquid
156.93
J/mol×K
309.15
Heat Ca...
Cp,liquid
157.38
J/mol×K
311.15
Heat Ca...
Cp,liquid
157.83
J/mol×K
313.15
Heat Ca...
Cp,liquid
158.28
J/mol×K
315.15
Heat Ca...
Cp,liquid
158.74
J/mol×K
317.15
Heat Ca...
Cp,liquid
159.20
J/mol×K
319.15
Heat Ca...
Cp,liquid
159.66
J/mol×K
321.15
Heat Ca...
Cp,liquid
160.13
J/mol×K
323.15
Heat Ca...
Cp,liquid
160.60
J/mol×K
325.15
Heat Ca...
Cp,liquid
161.06
J/mol×K
327.15
Heat Ca...
Cp,liquid
161.53
J/mol×K
329.15
Heat Ca...
Cp,liquid
162.00
J/mol×K
331.15
Heat Ca...
Cp,liquid
162.48
J/mol×K
333.15
Heat Ca...
Cp,liquid
162.95
J/mol×K
335.15
Heat Ca...
Cp,liquid
163.42
J/mol×K
337.15
Heat Ca...
Cp,liquid
163.89
J/mol×K
339.15
Heat Ca...
Cp,liquid
164.36
J/mol×K
341.15
Heat Ca...
Cp,liquid
164.83
J/mol×K
343.15
Heat Ca...
Cp,liquid
165.30
J/mol×K
345.15
Heat Ca...
Cp,liquid
165.76
J/mol×K
347.15
Heat Ca...
Cp,liquid
166.23
J/mol×K
349.15
Heat Ca...
Cp,liquid
166.69
J/mol×K
351.15
Heat Ca...
Cp,liquid
167.15
J/mol×K
353.15
Heat Ca...
η
[0.0008780; 0.0011640]
Pa×s
[293.00; 313.15]
η
0.0011640
Pa×s
293.00
Thermop...
η
0.0010410
Pa×s
298.15
Thermop...
η
0.0010820
Pa×s
298.15
Thermop...
η
0.0009844
Pa×s
303.00
Thermop...
η
0.0010146
Pa×s
303.15
Thermop...
η
0.0009640
Pa×s
308.15
Thermop...
η
0.0009540
Pa×s
308.15
Thermop...
η
0.0008786
Pa×s
313.00
Thermop...
η
0.0008780
Pa×s
313.15
Thermop...
Δfus H
[10.63; 10.70]
kJ/mol
[242.40; 242.43]
Δfus H
10.70
kJ/mol
242.40
NIST
Δfus H
10.70
kJ/mol
242.40
NIST
Δfus H
10.70
kJ/mol
242.40
NIST
Δfus H
10.63
kJ/mol
242.43
NIST
Δvap H
[42.30; 44.00]
kJ/mol
[293.00; 429.10]
Δvap H
44.00
kJ/mol
293.00
NIST
Δvap H
42.40
kJ/mol
378.00
NIST
Δvap H
42.30
kJ/mol
398.00
NIST
Δvap H
42.50
kJ/mol
429.10
KDB
Pvap
[0.13; 95.30]
kPa
[276.40; 426.85]
Pvap
0.13
kPa
276.40
Thermoc...
Pvap
0.15
kPa
278.30
Thermoc...
Pvap
0.20
kPa
282.20
Thermoc...
Pvap
0.21
kPa
283.10
Thermoc...
Pvap
0.25
kPa
285.40
Thermoc...
Pvap
0.25
kPa
286.20
Thermoc...
Pvap
0.30
kPa
288.30
Thermoc...
Pvap
0.32
kPa
289.30
Thermoc...
Pvap
0.35
kPa
291.40
Thermoc...
Pvap
0.38
kPa
292.40
Thermoc...
Pvap
0.40
kPa
293.20
Thermoc...
Pvap
0.44
kPa
294.40
Thermoc...
Pvap
0.46
kPa
295.50
Thermoc...
Pvap
0.52
kPa
297.40
Thermoc...
Pvap
0.64
kPa
300.40
Thermoc...
Pvap
0.76
kPa
303.40
Thermoc...
Pvap
95.30
kPa
426.85
Vapor-l...
n 0
[1.54970; 1.55770]
[293.15; 313.15]
n 0
1.55710
293.15
Excess ...
n 0
1.55710
298.15
Activit...
n 0
1.55710
298.15
(Vapor ...
n 0
1.55770
298.15
Density...
n 0
1.55610
303.15
Refract...
n 0
1.55460
303.15
Excess ...
n 0
1.55420
303.15
Density...
n 0
1.55140
308.15
Density...
n 0
1.55340
308.15
Refract...
n 0
1.54970
313.15
Refract...
ρl
[1441.22; 1495.52]
kg/m3
[293.00; 333.15]
ρl
1495.00
kg/m3
293.00
KDB
ρl
1495.52
kg/m3
293.15
Theoret...
ρl
1495.28
kg/m3
293.20
Isobari...
ρl
1495.23
kg/m3
293.20
Isobari...
ρl
1488.12
kg/m3
298.15
Densiti...
ρl
1481.52
kg/m3
303.15
Studies...
ρl
1481.40
kg/m3
303.15
Densiti...
ρl
1481.97
kg/m3
303.15
Theoret...
ρl
1474.58
kg/m3
308.15
Densiti...
ρl
1475.36
kg/m3
308.15
Studies...
ρl
1468.41
kg/m3
313.15
Theoret...
ρl
1468.02
kg/m3
313.15
Studies...
ρl
1461.36
kg/m3
318.15
Studies...
ρl
1454.85
kg/m3
323.15
Theoret...
ρl
1441.22
kg/m3
333.15
Theoret...
Δfus S
[43.84; 44.15]
J/mol×K
[242.40; 242.43]
Δfus S
44.15
J/mol×K
242.40
NIST
Δfus S
43.84
J/mol×K
242.43
NIST
γ
0.04
N/m
293.20
KDB
Pressure Dependent Properties
Datasets
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
248.15
99.70
1554.489
248.15
1231.41
1555.368
248.15
2075.45
1556.036
248.15
4196.22
1557.697
248.15
5950.98
1559.054
248.15
8068.32
1560.666
248.15
10015.40
1562.113
248.15
11951.60
1563.577
248.15
13994.80
1565.093
248.15
15940.30
1566.527
248.15
18145.00
1568.122
248.15
19946.50
1569.417
248.15
21965.00
1570.861
248.15
24135.90
1572.41
248.15
25864.70
1573.623
248.15
27917.30
1575.05
248.15
29850.30
1576.387
273.15
100.51
1520.557
273.15
1116.26
1521.447
273.15
2128.10
1522.34
273.15
4045.82
1524.026
273.15
5967.30
1525.66
273.15
8142.83
1527.515
273.15
10020.30
1529.109
273.15
11896.10
1530.677
273.15
13922.00
1532.353
273.15
16083.00
1534.134
273.15
18195.20
1535.834
273.15
20035.10
1537.31
273.15
21829.30
1538.747
273.15
23856.50
1540.342
273.15
25976.20
1542.017
273.15
28097.70
1543.651
273.15
29947.00
1545.093
293.15
101.93
1493.557
293.15
1239.69
1494.684
293.15
2010.73
1495.408
293.15
4059.70
1497.371
293.15
6007.85
1499.218
293.15
8079.77
1501.16
293.15
10000.80
1502.944
293.15
11960.00
1504.732
293.15
14168.60
1506.732
293.15
15878.80
1508.265
293.15
17960.30
1510.109
293.15
19999.40
1511.901
293.15
21880.00
1513.531
293.15
24122.20
1515.458
293.15
26141.00
1517.174
293.15
28060.50
1518.79
293.15
29992.70
1520.418
313.15
102.54
1466.553
313.15
2000.76
1468.587
313.15
4010.97
1470.712
313.15
6189.56
1473.0
313.15
7991.64
1474.858
313.15
10089.40
1477.007
313.15
12142.80
1479.063
313.15
14014.60
1480.929
313.15
16087.30
1482.944
313.15
18046.60
1484.852
313.15
20004.20
1486.73
313.15
22154.30
1488.763
313.15
23944.20
1490.446
313.15
26099.80
1492.424
313.15
28042.50
1494.215
313.15
29905.50
1495.902
333.15
100.42
1439.385
333.15
1115.03
1440.596
333.15
1943.37
1441.571
333.15
4094.54
1444.097
333.15
6114.22
1446.439
333.15
7927.80
1448.512
333.15
10021.70
1450.842
333.15
11958.50
1453.001
333.15
13999.00
1455.239
333.15
16048.70
1457.443
333.15
18155.70
1459.682
333.15
20007.80
1461.631
333.15
22157.50
1463.842
333.15
24129.60
1465.857
333.15
26094.50
1467.846
333.15
28018.50
1469.764
333.15
29890.30
1471.607
353.15
99.80
1411.936
353.15
1173.75
1413.368
353.15
1944.34
1414.39
353.15
3949.81
1417.013
353.15
5968.93
1419.612
353.15
7990.46
1422.164
353.15
9916.05
1424.555
353.15
11986.60
1427.088
353.15
14134.60
1429.674
353.15
15921.30
1431.797
353.15
18146.30
1434.386
353.15
19873.50
1436.374
353.15
22180.00
1438.986
353.15
23963.50
1440.977
353.15
26085.20
1443.316
353.15
28122.10
1445.529
353.15
29956.10
1447.501
373.15
98.54
1384.068
373.15
1150.11
1385.641
373.15
2174.39
1387.16
373.15
3917.65
1389.708
373.15
6182.40
1392.956
373.15
8042.69
1395.57
373.15
10003.40
1398.276
373.15
12007.70
1400.991
373.15
14086.40
1403.757
373.15
15912.60
1406.155
373.15
18065.60
1408.912
373.15
19882.10
1411.213
373.15
22174.10
1414.047
373.15
24052.60
1416.329
373.15
25897.20
1418.541
373.15
27711.00
1420.705
373.15
29530.80
1422.851
393.15
97.33
1355.66
393.15
1226.04
1357.559
393.15
2181.20
1359.152
393.15
3965.26
1362.078
393.15
6075.43
1365.466
393.15
8146.91
1368.751
393.15
9937.30
1371.465
393.15
11969.70
1374.529
393.15
14177.00
1377.777
393.15
15955.80
1380.344
393.15
18163.70
1383.473
393.15
20146.90
1386.231
393.15
22175.70
1388.998
393.15
23981.50
1391.424
393.15
26169.90
1394.302
393.15
28005.40
1396.697
393.15
29541.50
1398.685
413.15
99.45
1326.547
413.15
1202.85
1328.655
413.15
2177.13
1330.512
413.15
3915.54
1333.735
413.15
6185.52
1337.833
413.15
8176.14
1341.325
413.15
10032.40
1344.48
413.15
12103.60
1348.01
413.15
13991.80
1351.03
413.15
15890.50
1354.115
413.15
18162.20
1357.681
413.15
19933.00
1360.414
413.15
22150.20
1363.736
413.15
24133.10
1366.656
413.15
26038.90
1369.413
413.15
27898.50
1372.058
413.15
29858.00
1374.805
433.15
1243.75
1299.092
433.15
1973.28
1300.66
433.15
4075.91
1305.09
433.15
6197.75
1309.427
433.15
7981.47
1312.955
433.15
10019.80
1316.907
433.15
12072.60
1320.75
433.15
14033.50
1324.335
433.15
15960.20
1327.765
433.15
17921.10
1331.186
433.15
19992.20
1334.752
433.15
21950.20
1337.95
433.15
24017.90
1341.307
433.15
26143.40
1344.678
433.15
28052.40
1347.64
433.15
29864.50
1350.426
453.15
1135.36
1268.141
453.15
1982.45
1270.245
453.15
4017.67
1275.165
453.15
6189.02
1280.221
453.15
7994.19
1284.28
453.15
10138.80
1288.978
453.15
12157.20
1293.201
453.15
13981.80
1296.937
453.15
16133.80
1301.214
453.15
18121.60
1305.054
453.15
19974.20
1308.564
453.15
22140.80
1312.522
453.15
24115.40
1316.051
453.15
26121.30
1319.557
453.15
28034.20
1322.825
453.15
29912.10
1325.979
473.15
1191.19
1236.278
473.15
2175.44
1239.118
473.15
4131.48
1244.576
473.15
5988.10
1249.543
473.15
8161.41
1255.135
473.15
10165.40
1260.077
473.15
12165.90
1264.845
473.15
14162.70
1269.434
473.15
16124.70
1273.802
473.15
18166.70
1278.202
473.15
20146.20
1282.345
473.15
22123.10
1286.362
473.15
24157.00
1290.388
473.15
26074.70
1294.08
473.15
28019.90
1297.733
473.15
29860.30
1301.116
Reference
Correlations
Similar Compounds
Find more compounds similar to Benzene, bromo- .
Mixtures
Benzene, bromo- + Triethylene glycol
Benzene, bromo- + Methyl Alcohol
Benzene, bromo- + 1-Hexanol, 2-ethyl-
Benzene, bromo- + Heptane
Benzene, nitro- + Benzene, bromo-
Benzene, bromo- + Dimethyl Sulfoxide
Benzene, bromo- + Formamide, N,N-dimethyl-
Benzene, bromo- + N-Formylmorpholine
Acetonitrile + Benzene, bromo-
Benzene, bromo- + Ethane, 1,2-dichloro-
Benzene, bromo- + m-Chloroaniline
Acetic acid, pentyl ester + Benzene, bromo-
Acetic acid, chloro-, ethyl ester + Benzene, bromo-
Ethane, 1,2-dibromo- + Benzene, bromo-
Benzene, bromo- + Methyl formate
Ethyl formate + Benzene, bromo-
Formic acid, propyl ester + Benzene, bromo-
Acetic acid, phenylmethyl ester + Benzene, bromo-
Benzene, bromo- + Ethanol, 2-methoxy-
Benzene, bromo- + Benzene, chloro-
Find more mixtures with Benzene, bromo- .
Sources
KDB Pure (Korean Thermophysical Properties Databank)
KDB Vapor Pressure Data
Crippen Method
Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds at 95.5 kPa
Refractive properties, speed of sound and FT-IR study of binary mixtures of N-formylmorpholine with some halobenzenes at 303.15, 308.15 and 313.15 K
(Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
Measurement and correlation of the (p, ?, T) relation of liquid n-heptane, n-nonane, 2,4-dichlorotoluene, and bromobenzene in the temperature range from (233.15 to 473.15) K at pressures up to 30 MPa for use as density reference liquids
Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
Thermodynamics of solvation in propylene glycol and methyl cellosolve
Phase behavior of ionic liquids 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imides with halogenated benzenes
Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
Volumetric and electromagnetic properties of binary mixtures consist of benzene derivatives at different temperature and ternary mixtures with 1,2-dichloroethane at T = 293.15 K with application of the Prigogine-Flory-Patterson theory and PC-SAFT
Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
Solubilities of p-Tolylboronic Acid, Bromobenzene and 4-Phenyltoluene in Carbon Dioxide at Elevated Pressures
Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
Measuring the Aqueous Henry's Law Constant at Elevated Temperatures Using an Extended EPICS Technique
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
Solubility of Hydrofluorocarbons in Halobenzene Solvents
Thermochemistry of Halogen-Substituted Methylbenzenes
Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Excess Volumes of Binary Solutions of Methyl Formate, Ethyl Formate, Propyl Formate, and Benzyl Acetate with Bromo-, Chloro-, and Nitrobenzenes at (303.15, 308.15, and 313.15) K
Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Liquid-Liquid Equilibria in Binary Mixtures Containing Chlorobenzene, Bromobenzene, and Iodobenzene with Ionic Liquid 1-Ethyl-3-methylimidazolim Bis(trifluoromethylsulfonyl)imide
Joback Method
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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