Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
εr
[26.32; 36.21]
[248.15; 333.15]
εr
36.21
248.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
35.82
250.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
35.44
253.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
35.06
255.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
34.70
258.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
34.35
260.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
33.99
263.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
33.65
265.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
33.31
268.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
32.98
270.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
32.66
273.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
32.36
275.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
32.04
278.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
31.73
280.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
31.43
283.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
31.14
285.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
30.86
288.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
30.57
290.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
30.28
293.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
30.00
295.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
29.71
298.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
29.45
300.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
29.18
303.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
28.92
305.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
28.67
308.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
28.42
310.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
28.17
313.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
27.94
315.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
27.68
318.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
27.46
320.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
27.23
323.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
27.00
325.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
26.77
328.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
26.56
330.65
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
εr
26.32
333.15
Temperature Dependence of the Relative Static Permittivity of Homologous Series of Liquid 1,n-Dicyanoalkanes N=C (CH2)n C=N, n = 2 to 6
Δfus H
15.00
kJ/mol
241.70
NIST
Δvap H
74.50
kJ/mol
318.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
448.70
K
1.90
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[156.73; 333.42]
J/mol×K
[273.00; 1000.00]
Joback Predicted correlation
Equation Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A 3.05250e+01
Coefficient B 5.38400e-01
Coefficient C -2.95000e-04
Coefficient D 5.95000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
156.73
J/mol×K
273.00
Calculated Property
Cp,gas
186.71
J/mol×K
353.78
Calculated Property
Cp,gas
213.66
J/mol×K
434.56
Calculated Property
Cp,gas
237.78
J/mol×K
515.33
Calculated Property
Cp,gas
259.25
J/mol×K
596.11
Calculated Property
Cp,gas
278.25
J/mol×K
676.89
Calculated Property
Cp,gas
294.98
J/mol×K
757.67
Calculated Property
Cp,gas
309.63
J/mol×K
838.44
Calculated Property
Cp,gas
322.38
J/mol×K
919.22
Calculated Property
Cp,gas
333.42
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[2.77e-04; 2.33e-03]
kPa
[306.15; 330.15]
KDB Vapor Pressure Data
Equation ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A 1.64050e+02
Coefficient B -1.46677e+04
Coefficient C -2.20521e+01
Coefficient D 2.02482e-05
Coefficient E 0.00000e+00
Temperature range, min. 306.15
Temperature range, max. 330.15
Pvap
2.77e-04
kPa
306.15
Calculated Property
Pvap
3.58e-04
kPa
308.82
Calculated Property
Pvap
4.60e-04
kPa
311.48
Calculated Property
Pvap
5.88e-04
kPa
314.15
Calculated Property
Pvap
7.48e-04
kPa
316.82
Calculated Property
Pvap
9.47e-04
kPa
319.48
Calculated Property
Pvap
1.19e-03
kPa
322.15
Calculated Property
Pvap
1.50e-03
kPa
324.82
Calculated Property
Pvap
1.87e-03
kPa
327.48
Calculated Property
Pvap
2.33e-03
kPa
330.15
Calculated Property
Similar Compounds
Find more compounds similar to Heptanedinitrile .
Sources
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