- InChI
- InChI=1S/C2H6S2/c1-3-4-2/h1-2H3
- InChI Key
- WQOXQRCZOLPYPM-UHFFFAOYSA-N
- Formula
- C2H6S2
- SMILES
- CSSC
- Molecular Weight1
- 94.20
- CAS
- 624-92-0
- Other Names
-
- (CH3S)2
- (Methyldithio)methane
- 2,3-dithiabutane
- DMDS
- Dimethyl disulphide
- Methyldisulfanylmethane
- NSC 9370
- Sulfa-Hitech
- UN 2381
- dimethyl disulfide
- dimethyldisulfide
- disulfide, dimethyl-
- methyl disulfide
- 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).
- EA : Electron affinity (eV).
- 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).
- ΔfH°(+) ion : Enthalpy of formation of positive ion at standard conditions (kJ/mol).
- ΔfH(+) ion,0K : Enthalpy of formation of positive ion at 0K (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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : 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).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2380 | KDB | |
| PAff | 815.30 | kJ/mol | NIST |
| BasG | 782.80 | kJ/mol | NIST |
| ΔcH°liquid | -2786.50 ± 0.71 | kJ/mol | NIST |
| EA | [0.23; 1.75] | eV |
|
| EA | 1.75 | eV | NIST |
| EA | 0.23 ± 0.21 | eV | NIST |
| ΔfG° | 32.20 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-24.10; -24.00] | kJ/mol |
|
| ΔfH°gas | -24.10 ± 2.30 | kJ/mol | NIST |
| ΔfH°gas | -24.00 | kJ/mol | NIST |
| ΔfH°gas | -24.10 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | [-62.60; -62.47] | kJ/mol |
|
| ΔfH°liquid | -62.60 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -62.47 ± 0.84 | kJ/mol | NIST |
| ΔfH°(+) ion | 690.00 ± 15.00 | kJ/mol | NIST |
| ΔfH(+) ion,0K | 707.00 ± 15.00 | kJ/mol | NIST |
| ΔfusH° | 9.20 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [37.80; 38.50] | kJ/mol |
|
| ΔvapH° | 37.90 | kJ/mol | NIST |
| ΔvapH° | 38.50 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 38.50 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 38.50 | kJ/mol | NIST |
| ΔvapH° | 37.80 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 37.80 | kJ/mol | NIST |
| ΔvapH° | 38.40 | kJ/mol | NIST |
| ΔvapH° | 38.40 | kJ/mol | NIST |
| ΔvapH° | 38.40 ± 3.10 | kJ/mol | NIST |
| IE | [7.40; 9.00] | eV |
|
| IE | Outlier 7.40 ± 0.10 | eV | NIST |
| IE | 8.20 ± 0.20 | eV | NIST |
| IE | 8.18 ± 0.03 | eV | NIST |
| IE | Outlier 7.40 ± 0.30 | eV | NIST |
| IE | 8.33 ± 0.02 | eV | NIST |
| IE | 8.30 | eV | NIST |
| IE | 8.71 ± 0.03 | eV | NIST |
| IE | 8.46 ± 0.03 | eV | NIST |
| IE | 8.97 | eV | NIST |
| IE | 8.96 | eV | NIST |
| IE | 8.97 | eV | NIST |
| IE | 8.96 | eV | NIST |
| IE | 9.00 | eV | NIST |
| IE | 8.97 | eV | NIST |
| IE | 8.98 | eV | NIST |
| IE | 8.82 | eV | NIST |
| IE | 8.97 | eV | NIST |
| log10WS | [-1.44; -1.44] |
|
|
| log10WS | -1.44 | Aq. Solubility Prediction | |
| log10WS | -1.44 | Estimated Solubility | |
| logPoct/wat | 1.627 | Crippen Calculated Property | |
| McVol | 71.740 | ml/mol | McGowan Calculated Property |
| Pc | [4800.00; 5070.00] | kPa |
|
| Pc | 5070.00 | kPa | Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method |
| Pc | 4800.00 | kPa | KDB |
| Inp | [718.00; 785.00] |
|
|
| Inp | 758.50 | NIST | |
| Inp | Outlier 767.80 | NIST | |
| Inp | 747.10 | NIST | |
| Inp | 751.30 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | Outlier 777.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | Outlier 785.00 | NIST | |
| Inp | 747.90 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | Outlier 783.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | Outlier 783.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | Outlier 768.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | Outlier 770.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | Outlier 770.00 | NIST | |
| Inp | Outlier 770.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | Outlier 770.00 | NIST | |
| I | [1036.00; 1127.00] |
|
|
| I | 1105.00 | NIST | |
| I | 1078.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1081.00 | NIST | |
| I | 1069.00 | NIST | |
| I | 1076.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1060.00 | NIST | |
| I | 1068.00 | NIST | |
| I | Outlier 1036.00 | NIST | |
| I | 1071.00 | NIST | |
| I | Outlier 1112.00 | NIST | |
| I | 1062.00 | NIST | |
| I | 1078.00 | NIST | |
| I | 1050.00 | NIST | |
| I | 1095.00 | NIST | |
| I | 1086.00 | NIST | |
| I | 1105.00 | NIST | |
| I | Outlier 1036.00 | NIST | |
| I | 1086.00 | NIST | |
| I | 1054.00 | NIST | |
| I | 1071.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1074.00 | NIST | |
| I | 1066.00 | NIST | |
| I | 1062.00 | NIST | |
| I | Outlier 1113.00 | NIST | |
| I | 1074.00 | NIST | |
| I | 1074.00 | NIST | |
| I | 1074.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1104.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1058.00 | NIST | |
| I | Outlier 1110.00 | NIST | |
| I | 1057.00 | NIST | |
| I | 1063.00 | NIST | |
| I | 1081.00 | NIST | |
| I | Outlier 1120.00 | NIST | |
| I | 1078.00 | NIST | |
| I | 1078.00 | NIST | |
| I | 1076.00 | NIST | |
| I | 1055.00 | NIST | |
| I | Outlier 1037.00 | NIST | |
| I | 1077.00 | NIST | |
| I | Outlier 1037.00 | NIST | |
| I | Outlier 1039.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1081.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1072.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1080.00 | NIST | |
| I | 1072.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1060.00 | NIST | |
| I | 1069.00 | NIST | |
| I | 1094.00 | NIST | |
| I | 1094.00 | NIST | |
| I | 1094.00 | NIST | |
| I | 1103.00 | NIST | |
| I | 1086.00 | NIST | |
| I | Outlier 1127.00 | NIST | |
| I | 1102.90 | NIST | |
| I | 1070.00 | NIST | |
| I | 1053.00 | NIST | |
| I | 1076.00 | NIST | |
| I | 1079.00 | NIST | |
| I | 1051.00 | NIST | |
| I | 1086.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1086.00 | NIST | |
| I | 1061.00 | NIST | |
| I | 1089.00 | NIST | |
| I | 1088.00 | NIST | |
| I | 1095.00 | NIST | |
| I | 1066.00 | NIST | |
| I | 1072.00 | NIST | |
| I | 1095.00 | NIST | |
| I | 1061.00 | NIST | |
| I | 1071.00 | NIST | |
| I | 1064.00 | NIST | |
| I | 1080.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1054.00 | NIST | |
| I | 1079.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1083.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1080.00 | NIST | |
| I | 1052.00 | NIST | |
| I | 1052.00 | NIST | |
| I | 1076.00 | NIST | |
| I | 1070.00 | NIST | |
| I | 1082.00 | NIST | |
| I | 1083.00 | NIST | |
| I | 1067.00 | NIST | |
| I | 1063.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1072.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1079.00 | NIST | |
| I | 1079.00 | NIST | |
| I | 1079.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1080.00 | NIST | |
| I | 1091.00 | NIST | |
| I | 1066.00 | NIST | |
| I | 1081.00 | NIST | |
| I | 1071.00 | NIST | |
| I | 1062.00 | NIST | |
| I | 1095.00 | NIST | |
| I | 1069.00 | NIST | |
| I | 1095.00 | NIST | |
| I | 1081.00 | NIST | |
| I | 1070.00 | NIST | |
| I | Outlier 1119.00 | NIST | |
| I | 1070.00 | NIST | |
| I | 1083.00 | NIST | |
| I | 1085.00 | NIST | |
| I | 1091.00 | NIST | |
| I | 1081.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1069.00 | NIST | |
| I | 1078.00 | NIST | |
| I | 1065.00 | NIST | |
| I | Outlier 1112.00 | NIST | |
| I | 1086.00 | NIST | |
| I | 1071.00 | NIST | |
| I | 1062.00 | NIST | |
| I | Outlier 1110.00 | NIST | |
| I | 1077.00 | NIST | |
| I | 1072.00 | NIST | |
| I | 1060.00 | NIST | |
| I | 1103.00 | NIST | |
| I | 1053.00 | NIST | |
| I | 1079.00 | NIST | |
| I | 1061.00 | NIST | |
| I | 1080.00 | NIST | |
| I | 1070.00 | NIST | |
| S°liquid | 235.39 | J/mol×K | NIST |
| Tboil | [0.00; 383.00] | K |
|
| Tboil | 382.90 | K | KDB |
| Tboil | 382.90 | K | NIST |
| Tboil | 382.90 | K | NIST |
| Tboil | 381.15 ± 1.50 | K | NIST |
| Tboil | 383.00 ± 1.50 | K | NIST |
| Tboil | Outlier 0.00 | K | NIST |
| Tc | [605.00; 615.00] | K |
|
| Tc | 605.00 | K | KDB |
| Tc | 615.00 ± 50.00 | K | NIST |
| Tc | 605.70 | K | NIST |
| Tfus | [188.00; 188.50] | K |
|
| Tfus | 188.00 | K | KDB |
| Tfus | 188.50 ± 0.20 | K | NIST |
| Ttriple | [188.44; 188.44] | K |
|
| Ttriple | 188.44 ± 0.02 | K | NIST |
| Ttriple | 188.44 ± 0.02 | K | NIST |
| Vc | 0.265 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [107.13; 139.82] | J/mol×K | [382.92; 606.39] |
|
| Cp,gas | 107.13 | J/mol×K | 382.92 | Joback Calculated Property |
| Cp,gas | 113.03 | J/mol×K | 420.16 | Joback Calculated Property |
| Cp,gas | 118.76 | J/mol×K | 457.41 | Joback Calculated Property |
| Cp,gas | 124.32 | J/mol×K | 494.65 | Joback Calculated Property |
| Cp,gas | 129.69 | J/mol×K | 531.90 | Joback Calculated Property |
| Cp,gas | 134.86 | J/mol×K | 569.14 | Joback Calculated Property |
| Cp,gas | 139.82 | J/mol×K | 606.39 | Joback Calculated Property |
| Cp,liquid | 146.11 | J/mol×K | 298.15 | NIST |
| ΔfusH | [9.19; 9.19] | kJ/mol | [188.40; 188.44] |
|
| ΔfusH | 9.19 | kJ/mol | 188.40 | NIST |
| ΔfusH | 9.19 | kJ/mol | 188.40 | NIST |
| ΔfusH | 9.19 | kJ/mol | 188.44 | NIST |
| ΔfusH | 9.19 | kJ/mol | 188.44 | NIST |
| ΔvapH | [33.68; 38.20] | kJ/mol | [310.50; 383.00] |
|
| ΔvapH | 38.20 | kJ/mol | 310.50 | NIST |
| ΔvapH | 38.20 | kJ/mol | 310.50 | NIST |
| ΔvapH | 36.00 ± 0.10 | kJ/mol | 341.00 | NIST |
| ΔvapH | 37.80 | kJ/mol | 349.50 | NIST |
| ΔvapH | 36.70 | kJ/mol | 354.50 | NIST |
| ΔvapH | 34.90 ± 0.10 | kJ/mol | 360.00 | NIST |
| ΔvapH | 36.20 | kJ/mol | 367.50 | NIST |
| ΔvapH | 36.20 | kJ/mol | 367.50 | NIST |
| ΔvapH | 33.68 | kJ/mol | 382.90 | KDB |
| ΔvapH | 33.78 | kJ/mol | 382.90 | NIST |
| ΔvapH | 33.70 ± 0.10 | kJ/mol | 383.00 | NIST |
| Pvap | [18.20; 100.60] | kPa | [332.19; 382.02] |
|
| Pvap | 18.20 | kPa | 332.19 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| Pvap | 31.10 | kPa | 346.26 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| Pvap | 41.70 | kPa | 354.42 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| Pvap | 53.90 | kPa | 362.18 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| Pvap | 61.90 | kPa | 366.46 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| Pvap | 72.90 | kPa | 371.63 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| Pvap | 81.10 | kPa | 375.04 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| Pvap | 90.90 | kPa | 378.75 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| Pvap | 100.60 | kPa | 382.02 | Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K |
| n0 | 1.52260 | 298.00 | Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane | |
| ρl | 1051.14 | kg/m3 | 303.15 | Isobaric Vapor Liquid Equilibrium for the Binary Systems Dimethyl Disulfide + C1 C4 n-Alkanol at 40.000 and 101.325 kPa |
| ΔfusS | [48.78; 48.78] | J/mol×K | [188.44; 188.44] |
|
| ΔfusS | 48.78 | J/mol×K | 188.44 | NIST |
| ΔfusS | 48.78 | J/mol×K | 188.44 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 5897.21] | kPa | [279.68; 615.00] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.46948e+01 | |||
| Coefficient B | -3.46015e+03 | |||
| Coefficient C | -3.95090e+01 | |||
| Temperature range, min. | 279.68 | |||
| Temperature range, max. | 615.00 | |||
| Pvap | 1.33 | kPa | 279.68 | Calculated Property |
| Pvap | 9.23 | kPa | 316.94 | Calculated Property |
| Pvap | 40.42 | kPa | 354.20 | Calculated Property |
| Pvap | 129.44 | kPa | 391.45 | Calculated Property |
| Pvap | 331.75 | kPa | 428.71 | Calculated Property |
| Pvap | 721.33 | kPa | 465.97 | Calculated Property |
| Pvap | 1384.36 | kPa | 503.23 | Calculated Property |
| Pvap | 2411.31 | kPa | 540.48 | Calculated Property |
| Pvap | 3889.49 | kPa | 577.74 | Calculated Property |
| Pvap | 5897.21 | kPa | 615.00 | Calculated Property |
| Pvap | [1.95e-04; 5336.33] | kPa | [188.44; 606.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.00528e+01 | |||
| Coefficient B | -7.14948e+03 | |||
| Coefficient C | -9.71673e+00 | |||
| Coefficient D | 7.02902e-06 | |||
| Temperature range, min. | 188.44 | |||
| Temperature range, max. | 606.00 | |||
| Pvap | 1.95e-04 | kPa | 188.44 | Calculated Property |
| Pvap | 0.05 | kPa | 234.84 | Calculated Property |
| Pvap | 1.48 | kPa | 281.23 | Calculated Property |
| Pvap | 14.99 | kPa | 327.63 | Calculated Property |
| Pvap | 77.94 | kPa | 374.02 | Calculated Property |
| Pvap | 267.27 | kPa | 420.42 | Calculated Property |
| Pvap | 699.68 | kPa | 466.81 | Calculated Property |
| Pvap | 1531.63 | kPa | 513.21 | Calculated Property |
| Pvap | 2974.93 | kPa | 559.60 | Calculated Property |
| Pvap | 5336.33 | kPa | 606.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Disulfide, dimethyl.
Mixtures
- Toluene + Disulfide, dimethyl
- Disulfide, dimethyl + Pentane, 2,2,4-trimethyl-
- 1-Pentene, 2,4,4-trimethyl- + Disulfide, dimethyl
- sodium chloride + Disulfide, dimethyl + Water
- Disulfide, dimethyl + Water
- Disulfide, dimethyl + Methyl Alcohol
- Ethanol + Disulfide, dimethyl
- 1-Propanol + Disulfide, dimethyl
- 1-Butanol + Disulfide, dimethyl
- Butane + Disulfide, dimethyl
- Disulfide, dimethyl + Isobutane
- 1-Propene, 2-methyl- + Disulfide, dimethyl
- 2-Butene, (E)- + Disulfide, dimethyl
- Propane, 2-ethoxy-2-methyl- + Disulfide, dimethyl
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K
- Combined effects of salinity and temperature on the solubility of organic compounds
- Isobaric Vapor Liquid Equilibrium for the Binary Systems Dimethyl Disulfide + C1 C4 n-Alkanol at 40.000 and 101.325 kPa
- Liquid-Liquid Equilibria on Three Binary Systems: Methyl Cyclopropanecarboxalate + Water; Dimethyl Sulfide + Water; and Dimethyl Disulfide + Water
- Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method
- Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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