- InChI
- InChI=1S/C4H10S/c1-3-4-5-2/h3-4H2,1-2H3
- InChI Key
- ZOASGOXWEHUTKZ-UHFFFAOYSA-N
- Formula
- C4H10S
- SMILES
- CCCSC
- Molecular Weight1
- 90.19
- CAS
- 3877-15-4
- Other Names
-
- 1-(Methylthio)propane
- 2-Thiapentane
- Methyl propyl sulfide
- Methyl propyl sulphide
- Sulfide, methyl propyl
- methyl N-propyl sulfide
- n-C3H7SCH3
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- VCOSTALD : COSTALD Characteristic Volume (m3/kmol).
- ωSRK : SRK acentric factor.
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3569 | ChemSep v8.3 pure component data Compiled value | |
| μ | 1.65 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 17.93 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -81.90 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 10.25 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [36.20; 36.31] | kJ/mol |
|
| ΔvapH° | 36.31 | kJ/mol | NIST |
| ΔvapH° | 36.20 | kJ/mol | NIST |
| ΔvapH° | 36.30 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 36.30 ± 0.40 | kJ/mol | NIST |
| IE | 8.80 ± 0.15 | eV | NIST |
| log10WS | -1.51 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.759 | Crippen Calculated Property | |
| McVol | 83.570 | ml/mol | McGowan Calculated Property |
| Pc | 3800.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 4.26e-06 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [701.00; 752.00] |
|
|
| Inp | 715.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | Outlier 752.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 701.00 | NIST | |
| Inp | 702.00 | NIST | |
| Inp | 717.00 | NIST | |
| Ip | [951.00; 951.00] |
|
|
| Ip | 951.00 | NIST | |
| Ip | 951.00 | NIST | |
| S°liquid | 272.55 | J/mol×K | NIST |
| Tboil | [367.00; 368.80] | K |
|
| Tboil | 368.69 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 368.70 | K | NIST |
| Tboil | 368.70 | K | NIST |
| Tboil | 368.80 ± 0.30 | K | NIST |
| Tboil | 368.80 ± 0.30 | K | NIST |
| Tboil | Outlier 367.00 ± 3.00 | K | NIST |
| Tc | [552.00; 574.10] | K |
|
| Tc | 552.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 574.10 | K | NIST |
| Tfus | [160.15; 160.18] | K |
|
| Tfus | 160.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 160.17 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 160.18 ± 0.06 | K | NIST |
| Tfus | 160.17 ± 0.10 | K | NIST |
| Ttriple | [160.17; 160.18] | K |
|
| Ttriple | 160.18 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ttriple | 160.17 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 160.17 ± 0.05 | K | NIST |
| Ttriple | 160.17 ± 0.05 | K | NIST |
| UQi | 3.30 | ChemSep v8.3 pure component data Compiled value | |
| URi | 3.86 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.322 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| VCOSTALD | 0.31 | m3/kmol | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
| ωSRK | 0.28 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zc | 0.2590000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | [0.26; 0.27] |
|
|
| Zra | 0.27 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | 171.63 | J/mol×K | 298.15 | NIST |
| ΔfusH | [9.91; 9.91] | kJ/mol | [160.17; 160.20] |
|
| ΔfusH | 9.91 | kJ/mol | 160.17 | NIST |
| ΔfusH | 9.91 | kJ/mol | 160.17 | NIST |
| ΔfusH | 9.91 | kJ/mol | 160.20 | NIST |
| ΔfusH | 9.91 | kJ/mol | 160.20 | NIST |
| ΔvapH | [32.08; 35.30] | kJ/mol | [328.00; 369.00] |
|
| ΔvapH | 34.50 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 34.50 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 35.30 | kJ/mol | 341.00 | NIST |
| ΔvapH | 33.40 ± 0.10 | kJ/mol | 347.00 | NIST |
| ΔvapH | 33.40 ± 0.10 | kJ/mol | 347.00 | NIST |
| ΔvapH | 32.08 | kJ/mol | 368.70 | NIST |
| ΔvapH | 32.10 ± 0.10 | kJ/mol | 369.00 | NIST |
| ΔvapH | 32.10 ± 0.10 | kJ/mol | 369.00 | NIST |
| ΔfusS | [61.88; 61.88] | J/mol×K | [160.17; 160.17] |
|
| ΔfusS | 61.88 | J/mol×K | 160.17 | NIST |
| ΔfusS | 61.88 | J/mol×K | 160.17 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [110.42; 298.97] | J/mol×K | [273.15; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 7.62010e+01 | |||
| Coefficient B | -5.75500e+02 | |||
| Coefficient C | 5.56424e+00 | |||
| Coefficient D | 3.03730e-04 | |||
| Coefficient E | -1.02240e-07 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 110.42 | J/mol×K | 273.15 | Calculated Property |
| Cp,gas | 147.44 | J/mol×K | 409.47 | Calculated Property |
| Cp,gas | 180.28 | J/mol×K | 545.78 | Calculated Property |
| Cp,gas | 207.85 | J/mol×K | 682.10 | Calculated Property |
| Cp,gas | 230.85 | J/mol×K | 818.42 | Calculated Property |
| Cp,gas | 250.06 | J/mol×K | 954.73 | Calculated Property |
| Cp,gas | 266.09 | J/mol×K | 1091.05 | Calculated Property |
| Cp,gas | 279.39 | J/mol×K | 1227.37 | Calculated Property |
| Cp,gas | 290.27 | J/mol×K | 1363.68 | Calculated Property |
| Cp,gas | 298.97 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [158.14; 190.11] | J/mol×K | [160.17; 368.69] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.40680e+02 | |||
| Coefficient B | 4.77810e+02 | |||
| Coefficient C | -3.09686e+00 | |||
| Coefficient D | 2.09490e-02 | |||
| Coefficient E | -1.48770e-05 | |||
| Temperature range, min. | 160.17 | |||
| Temperature range, max. | 368.69 | |||
| Cp,liquid | 158.14 | J/mol×K | 160.17 | Calculated Property |
| Cp,liquid | 157.97 | J/mol×K | 183.34 | Calculated Property |
| Cp,liquid | 159.01 | J/mol×K | 206.51 | Calculated Property |
| Cp,liquid | 160.97 | J/mol×K | 229.68 | Calculated Property |
| Cp,liquid | 163.75 | J/mol×K | 252.85 | Calculated Property |
| Cp,liquid | 167.34 | J/mol×K | 276.01 | Calculated Property |
| Cp,liquid | 171.75 | J/mol×K | 299.18 | Calculated Property |
| Cp,liquid | 177.00 | J/mol×K | 322.35 | Calculated Property |
| Cp,liquid | 183.13 | J/mol×K | 345.52 | Calculated Property |
| Cp,liquid | 190.11 | J/mol×K | 368.69 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0071209; 0.0001422] | Pa×s | [160.17; 452.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.16830e+01 | |||
| Coefficient B | 9.83430e+02 | |||
| Coefficient C | 1.19960e-01 | |||
| Coefficient D | -4.12620e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 160.17 | |||
| Temperature range, max. | 452.00 | |||
| η | 0.0071209 | Pa×s | 160.17 | Calculated Property |
| η | 0.0025772 | Pa×s | 192.60 | Calculated Property |
| η | 0.0012510 | Pa×s | 225.02 | Calculated Property |
| η | 0.0007285 | Pa×s | 257.45 | Calculated Property |
| η | 0.0004785 | Pa×s | 289.87 | Calculated Property |
| η | 0.0003416 | Pa×s | 322.30 | Calculated Property |
| η | 0.0002591 | Pa×s | 354.72 | Calculated Property |
| η | 0.0002055 | Pa×s | 387.15 | Calculated Property |
| η | 0.0001687 | Pa×s | 419.57 | Calculated Property |
| η | 0.0001422 | Pa×s | 452.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [44.43; 11.03] | kJ/mol | [160.17; 543.69] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 5.46064e+01 | |||
| Coefficient B | 6.10381e-01 | |||
| Coefficient C | 1.83873e-01 | |||
| Coefficient D | -8.64255e-01 | |||
| Coefficient E | 4.48129e-01 | |||
| Critical temperature, Tc (K) | 5.52000e+02 | |||
| Temperature range, min. | 160.17 | |||
| Temperature range, max. | 543.69 | |||
| ΔvapH | 44.43 | kJ/mol | 160.17 | Calculated Property |
| ΔvapH | 41.80 | kJ/mol | 202.78 | Calculated Property |
| ΔvapH | 39.27 | kJ/mol | 245.40 | Calculated Property |
| ΔvapH | 36.81 | kJ/mol | 288.01 | Calculated Property |
| ΔvapH | 34.37 | kJ/mol | 330.62 | Calculated Property |
| ΔvapH | 31.85 | kJ/mol | 373.24 | Calculated Property |
| ΔvapH | 29.09 | kJ/mol | 415.85 | Calculated Property |
| ΔvapH | 25.74 | kJ/mol | 458.46 | Calculated Property |
| ΔvapH | 21.03 | kJ/mol | 501.08 | Calculated Property |
| ΔvapH | 11.03 | kJ/mol | 543.69 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [269.83; 393.44] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.42307e+01 | |||
| Coefficient B | -3.05990e+03 | |||
| Coefficient C | -5.03700e+01 | |||
| Temperature range, min. | 269.83 | |||
| Temperature range, max. | 393.44 | |||
| Pvap | 1.33 | kPa | 269.83 | Calculated Property |
| Pvap | 3.03 | kPa | 283.56 | Calculated Property |
| Pvap | 6.29 | kPa | 297.30 | Calculated Property |
| Pvap | 12.08 | kPa | 311.03 | Calculated Property |
| Pvap | 21.74 | kPa | 324.77 | Calculated Property |
| Pvap | 37.00 | kPa | 338.50 | Calculated Property |
| Pvap | 59.98 | kPa | 352.24 | Calculated Property |
| Pvap | 93.24 | kPa | 365.97 | Calculated Property |
| Pvap | 139.71 | kPa | 379.71 | Calculated Property |
| Pvap | 202.65 | kPa | 393.44 | Calculated Property |
| Pvap | [4.28e-06; 3390.45] | kPa | [160.17; 552.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.68819e+01 | |||
| Coefficient B | -6.78654e+03 | |||
| Coefficient C | -9.26788e+00 | |||
| Coefficient D | 6.74231e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 565 K. | |||
| Temperature range, min. | 160.17 | |||
| Temperature range, max. | 552.00 | |||
| Pvap | 4.28e-06 | kPa | 160.17 | Calculated Property |
| Pvap | 4.39e-03 | kPa | 203.71 | Calculated Property |
| Pvap | 0.29 | kPa | 247.24 | Calculated Property |
| Pvap | 4.67 | kPa | 290.78 | Calculated Property |
| Pvap | 32.14 | kPa | 334.32 | Calculated Property |
| Pvap | 132.10 | kPa | 377.85 | Calculated Property |
| Pvap | 388.81 | kPa | 421.39 | Calculated Property |
| Pvap | 916.12 | kPa | 464.93 | Calculated Property |
| Pvap | 1855.91 | kPa | 508.46 | Calculated Property |
| Pvap | 3390.45 | kPa | 552.00 | Calculated Property |
| Pvap | [1.34; 3876.69] | kPa | [269.15; 563.00] |
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 | 8.08044e+01 | |||
| Coefficient B | -6.94795e+03 | |||
| Coefficient C | -9.86974e+00 | |||
| Coefficient D | 7.27846e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 269.15 | |||
| Temperature range, max. | 563.00 | |||
| Pvap | 1.34 | kPa | 269.15 | Calculated Property |
| Pvap | 8.10 | kPa | 301.80 | Calculated Property |
| Pvap | 32.35 | kPa | 334.45 | Calculated Property |
| Pvap | 96.70 | kPa | 367.10 | Calculated Property |
| Pvap | 234.81 | kPa | 399.75 | Calculated Property |
| Pvap | 489.82 | kPa | 432.40 | Calculated Property |
| Pvap | 913.22 | kPa | 465.05 | Calculated Property |
| Pvap | 1565.86 | kPa | 497.70 | Calculated Property |
| Pvap | 2521.99 | kPa | 530.35 | Calculated Property |
| Pvap | 3876.69 | kPa | 563.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [966.51; 473.88] | kg/m3 | [160.17; 543.69] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 1.37806e+02 | |||
| Coefficient B | 3.53280e-01 | |||
| Coefficient C | 5.52000e+02 | |||
| Coefficient D | 3.99530e-01 | |||
| Temperature range, min. | 160.17 | |||
| Temperature range, max. | 543.69 | |||
| ρl | 966.51 | kg/m3 | 160.17 | Calculated Property |
| ρl | 927.87 | kg/m3 | 202.78 | Calculated Property |
| ρl | 888.02 | kg/m3 | 245.40 | Calculated Property |
| ρl | 846.62 | kg/m3 | 288.01 | Calculated Property |
| ρl | 803.21 | kg/m3 | 330.62 | Calculated Property |
| ρl | 757.09 | kg/m3 | 373.24 | Calculated Property |
| ρl | 707.06 | kg/m3 | 415.85 | Calculated Property |
| ρl | 650.85 | kg/m3 | 458.46 | Calculated Property |
| ρl | 582.82 | kg/m3 | 501.08 | Calculated Property |
| ρl | 473.88 | kg/m3 | 543.69 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 1.54e-04] | N/m | [160.17; 543.69] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -7.02370e-03 | |||
| Coefficient B | 9.27450e+01 | |||
| Coefficient C | -3.87050e+00 | |||
| Coefficient D | 3.56870e-03 | |||
| Coefficient E | -1.07480e-05 | |||
| Temperature range, min. | 160.17 | |||
| Temperature range, max. | 543.69 | |||
| γ | 0.04 | N/m | 160.17 | Calculated Property |
| γ | 0.04 | N/m | 202.78 | Calculated Property |
| γ | 0.03 | N/m | 245.40 | Calculated Property |
| γ | 0.03 | N/m | 288.01 | Calculated Property |
| γ | 0.02 | N/m | 330.62 | Calculated Property |
| γ | 0.02 | N/m | 373.24 | Calculated Property |
| γ | 0.01 | N/m | 415.85 | Calculated Property |
| γ | 0.01 | N/m | 458.46 | Calculated Property |
| γ | 0.00 | N/m | 501.08 | Calculated Property |
| γ | 1.54e-04 | N/m | 543.69 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.08] | W/m×K | [368.69; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 2.33040e-03 | |||
| Coefficient B | 6.75860e-01 | |||
| Coefficient C | 1.80330e+03 | |||
| Coefficient D | 1.53300e+05 | |||
| Temperature range, min. | 368.69 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 368.69 | Calculated Property |
| λgas | 0.02 | W/m×K | 438.84 | Calculated Property |
| λgas | 0.03 | W/m×K | 508.98 | Calculated Property |
| λgas | 0.04 | W/m×K | 579.13 | Calculated Property |
| λgas | 0.04 | W/m×K | 649.27 | Calculated Property |
| λgas | 0.05 | W/m×K | 719.42 | Calculated Property |
| λgas | 0.06 | W/m×K | 789.56 | Calculated Property |
| λgas | 0.07 | W/m×K | 859.71 | Calculated Property |
| λgas | 0.08 | W/m×K | 929.85 | Calculated Property |
| λgas | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.17; 0.11] | W/m×K | [160.17; 368.69] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -6.20590e-02 | |||
| Coefficient B | 3.08140e+00 | |||
| Coefficient C | -1.36290e+00 | |||
| Coefficient D | -5.52140e-04 | |||
| Coefficient E | -1.27830e-06 | |||
| Temperature range, min. | 160.17 | |||
| Temperature range, max. | 368.69 | |||
| λliquid | 0.17 | W/m×K | 160.17 | Calculated Property |
| λliquid | 0.16 | W/m×K | 183.34 | Calculated Property |
| λliquid | 0.16 | W/m×K | 206.51 | Calculated Property |
| λliquid | 0.15 | W/m×K | 229.68 | Calculated Property |
| λliquid | 0.15 | W/m×K | 252.85 | Calculated Property |
| λliquid | 0.14 | W/m×K | 276.01 | Calculated Property |
| λliquid | 0.13 | W/m×K | 299.18 | Calculated Property |
| λliquid | 0.13 | W/m×K | 322.35 | Calculated Property |
| λliquid | 0.12 | W/m×K | 345.52 | Calculated Property |
| λliquid | 0.11 | W/m×K | 368.69 | Calculated Property |
Similar Compounds
![2-[Propylthio]ethanal.](data:image/png;base64,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)
Find more compounds similar to Propane, 1-(methylthio)-.
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.
- 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)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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