- InChI
- InChI=1S/C8H18S/c1-3-5-7-9-8-6-4-2/h3-8H2,1-2H3
- InChI Key
- HTIRHQRTDBPHNZ-UHFFFAOYSA-N
- Formula
- C8H18S
- SMILES
- CCCCSCCCC
- Molecular Weight1
- 146.30
- CAS
- 544-40-1
- Other Names
-
- (n-C4H9)2S
- 1,1'-Thiobisbutane
- 5-thianonane
- Butyl monosulfide
- Di-n-butyl sulfide
- Dibutyl sulphide
- Dibutylsulfide
- NSC 8460
- Sulfide, n-butyl-
- Thianonane-5
- Thiononane-5
- butyl sulfide
- butylthiobutane
- dibutyl sulfide
- dibutyl thioether
- n-Butyl sulfide
- n-Dibutyl sulfide
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- VCOSTALD : COSTALD Characteristic Volume (m3/kmol).
- ωSRK : SRK acentric factor.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4277 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| PAff | 871.80 | kJ/mol | NIST |
| BasG | 842.10 | kJ/mol | NIST |
| ΔcH°liquid | [-6102.03; -6102.00] | kJ/mol |
|
| ΔcH°liquid | -6102.03 | kJ/mol | NIST |
| ΔcH°liquid | -6102.00 ± 1.30 | kJ/mol | NIST |
| ΔfG° | 49.60 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-167.40; -167.20] | kJ/mol |
|
| ΔfH°gas | -167.40 | kJ/mol | NIST |
| ΔfH°gas | -167.20 | kJ/mol | NIST |
| ΔfH°liquid | [-220.70; -220.50] | kJ/mol |
|
| ΔfH°liquid | -220.70 ± 1.90 | kJ/mol | NIST |
| ΔfH°liquid | -220.50 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | 20.61 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [40.30; 54.20] | kJ/mol |
|
| ΔvapH° | 52.96 | kJ/mol | NIST |
| ΔvapH° | Outlier 40.30 | kJ/mol | NIST |
| ΔvapH° | 53.00 | kJ/mol | NIST |
| ΔvapH° | 54.20 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 53.35 | kJ/mol | NIST |
| ΔvapH° | 53.35 | kJ/mol | NIST |
| IE | [8.20; 8.40] | eV |
|
| IE | 8.20 | eV | NIST |
| IE | 8.40 ± 0.05 | eV | NIST |
| IE | 8.22 | eV | NIST |
| log10WS | -3.88 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.320 | Crippen Calculated Property | |
| McVol | 139.930 | ml/mol | McGowan Calculated Property |
| Pc | [2480.00; 2499.69] | kPa |
|
| Pc | 2480.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 Compiled value |
| Pc | 2499.69 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Inp | [1050.00; 1092.00] |
|
|
| Inp | 1084.40 | NIST | |
| Inp | 1088.50 | NIST | |
| Inp | 1078.10 | NIST | |
| Inp | 1081.30 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1084.40 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Ip | [1254.00; 1289.00] |
|
|
| Ip | 1270.60 | NIST | |
| Ip | 1256.60 | NIST | |
| Ip | 1286.00 | NIST | |
| Ip | 1289.00 | NIST | |
| Ip | 1262.00 | NIST | |
| Ip | 1270.00 | NIST | |
| Ip | 1254.00 | NIST | |
| Ip | 1270.00 | NIST | |
| Ip | 1256.00 | NIST | |
| Ip | 1270.00 | NIST | |
| S°liquid | 405.09 | J/mol×K | NIST |
| Tboil | [458.20; 461.95] | K |
|
| Tboil | 461.70 | K | NIST |
| Tboil | 461.95 ± 0.30 | K | NIST |
| Tboil | 458.20 ± 0.60 | K | NIST |
| Tc | [650.00; 650.00] | K |
|
| Tc | 650.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 Compiled value |
| Tc | 650.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tfus | [193.15; 221.85] | K |
|
| Tfus | 193.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 221.85 | K | KDB |
| Tfus | 198.12 ± 0.02 | K | NIST |
| Ttriple | [198.13; 198.14] | K |
|
| Ttriple | 198.14 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ttriple | 198.13 ± 0.04 | K | NIST |
| Ttriple | 198.13 ± 0.03 | K | NIST |
| Ttriple | 198.13 ± 0.04 | K | NIST |
| Ttriple | 198.13 ± 0.03 | K | NIST |
| Vc | 0.536 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| VCOSTALD | 0.56 | m3/kmol | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
| ωSRK | 0.48 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zra | 0.26 | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | 284.34 | J/mol×K | 298.15 | NIST |
| ΔfusH | [19.41; 19.43] | kJ/mol | [198.10; 198.13] |
|
| ΔfusH | 19.41 | kJ/mol | 198.10 | NIST |
| ΔfusH | 19.41 | kJ/mol | 198.10 | NIST |
| ΔfusH | 19.43 | kJ/mol | 198.13 | NIST |
| ΔfusH | 19.43 | kJ/mol | 198.13 | NIST |
| ΔvapH | [44.80; 46.50] | kJ/mol | [338.50; 430.00] |
|
| ΔvapH | 44.80 | kJ/mol | 338.50 | NIST |
| ΔvapH | 46.50 | kJ/mol | 430.00 | NIST |
| ΔfusS | [98.05; 98.05] | J/mol×K | [198.13; 198.13] |
|
| ΔfusS | 98.05 | J/mol×K | 198.13 | NIST |
| ΔfusS | 98.05 | J/mol×K | 198.13 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [195.70; 458.65] | 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 | 1.52160e+01 | |||
| Coefficient B | 7.58230e-01 | |||
| Coefficient C | -3.71200e-04 | |||
| Coefficient D | 5.64000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 195.70 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 239.50 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 279.24 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 315.10 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 347.25 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 375.87 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 401.14 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 423.24 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 442.35 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 458.65 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [340.12; 492.01] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.43227e+01 | |||
| Coefficient B | -3.82370e+03 | |||
| Coefficient C | -6.76820e+01 | |||
| Temperature range, min. | 340.12 | |||
| Temperature range, max. | 492.01 | |||
| Pvap | 1.33 | kPa | 340.12 | Calculated Property |
| Pvap | 3.02 | kPa | 357.00 | Calculated Property |
| Pvap | 6.26 | kPa | 373.87 | Calculated Property |
| Pvap | 12.03 | kPa | 390.75 | Calculated Property |
| Pvap | 21.64 | kPa | 407.63 | Calculated Property |
| Pvap | 36.84 | kPa | 424.50 | Calculated Property |
| Pvap | 59.78 | kPa | 441.38 | Calculated Property |
| Pvap | 93.02 | kPa | 458.26 | Calculated Property |
| Pvap | 139.53 | kPa | 475.13 | Calculated Property |
| Pvap | 202.66 | kPa | 492.01 | Calculated Property |
| Pvap | [0.12; 2648.39] | kPa | [303.15; 650.00] |
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 | 2.52296e+02 | |||
| Coefficient B | -1.67842e+04 | |||
| Coefficient C | -3.51983e+01 | |||
| Coefficient D | 2.22154e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 303.15 | |||
| Temperature range, max. | 650.00 | |||
| Pvap | 0.12 | kPa | 303.15 | Calculated Property |
| Pvap | 1.53 | kPa | 341.69 | Calculated Property |
| Pvap | 9.59 | kPa | 380.23 | Calculated Property |
| Pvap | 36.91 | kPa | 418.77 | Calculated Property |
| Pvap | 103.29 | kPa | 457.31 | Calculated Property |
| Pvap | 234.69 | kPa | 495.84 | Calculated Property |
| Pvap | 467.25 | kPa | 534.38 | Calculated Property |
| Pvap | 859.69 | kPa | 572.92 | Calculated Property |
| Pvap | 1518.64 | kPa | 611.46 | Calculated Property |
| Pvap | 2648.39 | kPa | 650.00 | Calculated Property |
| Pvap | [3.79; 15.74] | kPa | [283.00; 313.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39436e+01 | |||
| Coefficient B | -2.97518e+03 | |||
| Coefficient C | -4.70660e+01 | |||
| Reference | Bauer and Burschkies, 1935 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 283.00 | |||
| Temperature range, max. | 313.00 | |||
| Pvap | 3.79 | kPa | 283.00 | Calculated Property |
| Pvap | 4.52 | kPa | 286.33 | Calculated Property |
| Pvap | 5.37 | kPa | 289.67 | Calculated Property |
| Pvap | 6.34 | kPa | 293.00 | Calculated Property |
| Pvap | 7.45 | kPa | 296.33 | Calculated Property |
| Pvap | 8.72 | kPa | 299.67 | Calculated Property |
| Pvap | 10.16 | kPa | 303.00 | Calculated Property |
| Pvap | 11.80 | kPa | 306.33 | Calculated Property |
| Pvap | 13.65 | kPa | 309.67 | Calculated Property |
| Pvap | 15.74 | kPa | 313.00 | Calculated Property |
Similar Compounds
![2-[Butylthio]ethanal.](data:image/png;base64,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)
![Butane, 1-[(1-methylethyl)thio]-.](data:image/png;base64,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)
Find more compounds similar to Butane, 1,1'-thiobis-.
Mixtures
Sources
- KDB Vapor Pressure Data
- 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).
- Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 8. Organic Sulfur, Silicon, and Tin Compounds (C + H + S, Si, and Sn). J. Chem. Eng. Data 2001, 46, 480-485.
- 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.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Liquid-Liquid Equilibria of Ternary Systems Sulfide + Octane + Solvents at Different Temperatures
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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