Physical Properties
Property
Value
Unit
Source
ω
0.4145
PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
PAff
846.40
kJ/mol
NIST
BasG
816.20
kJ/mol
NIST
IE
[9.59; 9.88]
eV
IE
9.60 ± 1.00
eV
NIST
IE
9.64 ± 0.01
eV
NIST
IE
9.59 ± 0.04
eV
NIST
IE
9.88
eV
NIST
log Poct/wat
2.673
Crippen Calculated Property
Pc
[1909.98; 1925.00]
kPa
Pc
1920.00
kPa
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 Compiled value
Pc
1909.98
kPa
PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc
1925.00 ± 10.00
kPa
NIST
Inp
[597.40; 646.00]
Inp
597.40
NIST
Inp
597.40
NIST
Inp
598.00
NIST
Inp
645.00
NIST
Inp
646.00
NIST
S°liquid
[433.80; 433.84]
J/mol×K
S°liquid
433.80
J/mol×K
NIST
S°liquid
433.84
J/mol×K
NIST
Tboil
[372.00; 375.00]
K
Tboil
374.12
K
Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
Tboil
374.00
K
NIST
Tboil
372.50 ± 0.50
K
NIST
Tboil
374.14 ± 0.30
K
NIST
Tboil
373.20 ± 1.50
K
NIST
Tboil
375.00 ± 3.00
K
NIST
Tboil
373.00 ± 3.00
K
NIST
Tboil
372.00 ± 3.00
K
NIST
Tc
[516.60; 518.70]
K
Tc
518.00
K
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 Compiled value
Tc
516.60
K
PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc
518.70 ± 0.51
K
NIST
Tfus
207.15
K
Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Ttriple
[204.93; 204.94]
K
Ttriple
204.94
K
Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple
204.93 ± 0.02
K
NIST
Ttriple
204.93 ± 0.02
K
NIST
Vc
[0.590; 0.620]
m3 /kmol
Vc
0.590
m3 /kmol
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 Compiled value
Vc
0.620
m3 /kmol
PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vm
2.14e-04
m3 /mol
Thermodynamic Study of Heptane + Silicone Mixtures. Excess Volumes and Enthalpies at 298.15 K
Zc
0.2630000
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 Compiled value
Cheméo can also estimate Enthalpy of formation at standard conditions , Enthalpy of vaporization at standard conditions , Standard Gibbs free energy of formation , Log10 of Water solubility in mol/l
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Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,liquid
[311.37; 311.40]
J/mol×K
[298.15; 298.15]
Cp,liquid
311.40
J/mol×K
298.15
NIST
Cp,liquid
311.37
J/mol×K
298.15
NIST
Δfus H
[11.92; 11.92]
kJ/mol
[204.90; 204.93]
Δfus H
11.92
kJ/mol
204.90
NIST
Δfus H
11.92
kJ/mol
204.90
NIST
Δfus H
11.92
kJ/mol
204.93
NIST
Δfus H
11.92
kJ/mol
204.93
NIST
Δfus H
11.92
kJ/mol
204.93
NIST
Δvap H
[31.30; 36.90]
kJ/mol
[327.00; 373.00]
Δvap H
33.10
kJ/mol
327.00
NIST
Δvap H
34.60 ± 0.10
kJ/mol
332.00
NIST
Δvap H
34.60 ± 0.10
kJ/mol
332.00
NIST
Δvap H
36.90
kJ/mol
341.50
NIST
Δvap H
33.10 ± 0.10
kJ/mol
351.00
NIST
Δvap H
33.10 ± 0.10
kJ/mol
351.00
NIST
Δvap H
36.00
kJ/mol
360.00
NIST
Δvap H
36.00
kJ/mol
360.00
NIST
Δvap H
31.30 ± 0.10
kJ/mol
373.00
NIST
Δvap H
31.30 ± 0.10
kJ/mol
373.00
NIST
Pvap
101.30
kPa
374.12
Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
n 0
1.37370
298.15
Determination and Correlation of Vapor Liquid Equilibrium Data for the Ethyl Acetate + Hexamethyl Disiloxane System at 101.3 kPa
ρl
[726.05; 763.87]
kg/m3
[293.15; 328.15]
ρl
763.87
kg/m3
293.15
The mixing properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl) cyclotrisiloxane with various organosilicon compounds at different temperatures
ρl
747.95
kg/m3
308.15
The mixing properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl) cyclotrisiloxane with various organosilicon compounds at different temperatures
ρl
742.53
kg/m3
313.15
The mixing properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl) cyclotrisiloxane with various organosilicon compounds at different temperatures
ρl
737.07
kg/m3
318.15
The mixing properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl) cyclotrisiloxane with various organosilicon compounds at different temperatures
ρl
731.57
kg/m3
323.15
The mixing properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl) cyclotrisiloxane with various organosilicon compounds at different temperatures
ρl
726.05
kg/m3
328.15
The mixing properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl) cyclotrisiloxane with various organosilicon compounds at different temperatures
Δfus S
[58.18; 58.18]
J/mol×K
[204.93; 204.93]
Δfus S
58.18
J/mol×K
204.93
NIST
Δfus S
58.18
J/mol×K
204.93
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[273.82; 398.55]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.40019e+01
Coefficient B -2.95909e+03
Coefficient C -5.80520e+01
Temperature range, min. 273.82
Temperature range, max. 398.55
Pvap
1.33
kPa
273.82
Calculated Property
Pvap
3.05
kPa
287.68
Calculated Property
Pvap
6.35
kPa
301.54
Calculated Property
Pvap
12.22
kPa
315.40
Calculated Property
Pvap
22.00
kPa
329.26
Calculated Property
Pvap
37.39
kPa
343.11
Calculated Property
Pvap
60.50
kPa
356.97
Calculated Property
Pvap
93.81
kPa
370.83
Calculated Property
Pvap
140.15
kPa
384.69
Calculated Property
Pvap
202.64
kPa
398.55
Calculated Property
Pvap
[9.61; 270.00]
kPa
[309.40; 411.56]
NIST
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.35898e+01
Coefficient B -2.77212e+03
Coefficient C -6.46730e+01
Reference Scott, Messerly, et al., 1961
Comment Coefficents calculated by NIST from author's data.
Temperature range, min. 309.40
Temperature range, max. 411.56
Pvap
9.61
kPa
309.40
Calculated Property
Pvap
15.87
kPa
320.75
Calculated Property
Pvap
25.13
kPa
332.10
Calculated Property
Pvap
38.32
kPa
343.45
Calculated Property
Pvap
56.55
kPa
354.80
Calculated Property
Pvap
81.03
kPa
366.16
Calculated Property
Pvap
113.13
kPa
377.51
Calculated Property
Pvap
154.28
kPa
388.86
Calculated Property
Pvap
206.04
kPa
400.21
Calculated Property
Pvap
270.00
kPa
411.56
Calculated Property
Pvap
[9.61; 270.00]
kPa
[309.40; 411.56]
NIST
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.35898e+01
Coefficient B -2.77212e+03
Coefficient C -6.46730e+01
Reference Scott, Messerly, et al., 1961, 2
Comment Coefficents calculated by NIST from author's data.
Temperature range, min. 309.40
Temperature range, max. 411.56
Pvap
9.61
kPa
309.40
Calculated Property
Pvap
15.87
kPa
320.75
Calculated Property
Pvap
25.13
kPa
332.10
Calculated Property
Pvap
38.32
kPa
343.45
Calculated Property
Pvap
56.55
kPa
354.80
Calculated Property
Pvap
81.03
kPa
366.16
Calculated Property
Pvap
113.13
kPa
377.51
Calculated Property
Pvap
154.28
kPa
388.86
Calculated Property
Pvap
206.04
kPa
400.21
Calculated Property
Pvap
270.00
kPa
411.56
Calculated Property
Property
Value
Unit
Temperature (K)
Source
γ
[0.02; 0.01]
N/m
[206.15; 374.15]
Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A 3.78513e-02
Coefficient B -7.63000e-05
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Temperature range, min. 206.15
Temperature range, max. 374.15
γ
0.02
N/m
206.15
Calculated Property
γ
0.02
N/m
224.82
Calculated Property
γ
0.02
N/m
243.48
Calculated Property
γ
0.02
N/m
262.15
Calculated Property
γ
0.02
N/m
280.82
Calculated Property
γ
0.02
N/m
299.48
Calculated Property
γ
0.01
N/m
318.15
Calculated Property
γ
0.01
N/m
336.82
Calculated Property
γ
0.01
N/m
355.48
Calculated Property
γ
0.01
N/m
374.15
Calculated Property
Similar Compounds
Find more compounds similar to Disiloxane, hexamethyl- .
Mixtures
Disiloxane, hexamethyl- + 2,4,6-trimethyl-2,4,6-tris(3,3,3-trifluoropropyl)-1,3,5,2,4,6-trioxatrisilinane
Disiloxane, hexamethyl- + Heptane
Disiloxane, hexamethyl- + Isopropyl acetate
Disiloxane, hexamethyl- + Acetone
Disiloxane, hexamethyl- + Acetone + Ethyl Acetate
Disiloxane, hexamethyl- + Trisiloxane, octamethyl-
Disiloxane, hexamethyl- + Tetrasiloxane, decamethyl-
Disiloxane, hexamethyl- + Pentasiloxane, dodecamethyl-
Disiloxane, hexamethyl- + Ethyl Acetate
Sources
Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C.; Nikitin, E. D. Vapor-Liquid Critical Properties of Elements and Compounds. 11. Organic Compounds Containing B + O; Halogens + N, + O, + O + S, + S, + Si; N + O; and O + S, + Si. J. Chem. Eng. Data 2009, 54, 669-689.
Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
Crippen Method
Crippen Method
The mixing properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl) cyclotrisiloxane with various organosilicon compounds at different temperatures
Bubble-Point Measurements and Modeling of Binary Mixtures of Linear Siloxanes
Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
Thermodynamic Study of Heptane + Silicone Mixtures. Excess Volumes and Enthalpies at 298.15 K
Determination and Correlation of Vapor Liquid Equilibrium Data for the Ethyl Acetate + Hexamethyl Disiloxane System at 101.3 kPa
Octanol/Air Partition Coefficients of Volatile Methylsiloxanes and Their Temperature Dependence
Isobaric Vapor Liquid Equilibrium for the Binary System of Hexamethyl Disiloxane + Isopropyl Acetate at Atmospheric Pressure
NIST Webbook
The Yaws Handbook of Vapor Pressure
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