- InChI
- InChI=1S/C7H14/c1-6-3-4-7(2)5-6/h6-7H,3-5H2,1-2H3/t6-,7+
- InChI Key
- XAZKFISIRYLAEE-KNVOCYPGSA-N
- Formula
- C7H14
- SMILES
- CC1CCC(C)C1
- Molecular Weight1
- 98.19
- CAS
- 2532-58-3
- Other Names
-
- 1,3-Dimethylcyclopentane cis
- 1,CIS-3-DIMETHYLCYCLOPENTANE
- 1-cis-3-Dimethylcyclopentane
- c-1,3-Dimethylcyclopentane
- cis-1,3-Dimethylcyclopentane
- ω : Acentric Factor.
- 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).
- 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).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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.
- 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 | [0.2760; 0.2975] |
|
|
| ω | 0.2975 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.2760 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | -4587.30 ± 1.40 | kJ/mol | NIST |
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 39.20 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-135.85; -133.60] | kJ/mol |
|
| ΔfH°gas | -135.85 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -133.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | -168.20 ± 1.40 | kJ/mol | NIST |
| ΔfusH° | 8.89 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [34.20; 34.60] | kJ/mol |
|
| ΔvapH° | 34.30 | kJ/mol | NIST |
| ΔvapH° | 34.30 | kJ/mol | NIST |
| ΔvapH° | 34.20 | kJ/mol | NIST |
| ΔvapH° | 34.60 | kJ/mol | NIST |
| IE | 9.47 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.29 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.442 | Crippen Calculated Property | |
| McVol | 98.630 | ml/mol | McGowan Calculated Property |
| Pc | [3400.00; 3543.91] | kPa |
|
| Pc | 3543.91 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 3400.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 1.73e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [674.96; 694.00] |
|
|
| Inp | 680.40 | NIST | |
| Inp | 683.90 | NIST | |
| Inp | Outlier 675.00 | NIST | |
| Inp | 687.30 | NIST | |
| Inp | 685.50 | NIST | |
| Inp | 685.60 | NIST | |
| Inp | 685.60 | NIST | |
| Inp | 685.80 | NIST | |
| Inp | 685.30 | NIST | |
| Inp | 683.30 | NIST | |
| Inp | 687.50 | NIST | |
| Inp | 682.70 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 681.90 | NIST | |
| Inp | 685.40 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 681.70 | NIST | |
| Inp | 683.40 | NIST | |
| Inp | 685.10 | NIST | |
| Inp | 686.80 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 685.50 | NIST | |
| Inp | 685.80 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 682.90 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | Outlier 692.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 683.50 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | Outlier 694.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 681.50 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 680.80 | NIST | |
| Inp | Outlier 674.96 | NIST | |
| Inp | Outlier 675.65 | NIST | |
| Inp | 687.90 | NIST | |
| Inp | 679.90 | NIST | |
| Inp | 677.60 | NIST | |
| Inp | 677.66 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 677.50 | NIST | |
| Inp | 677.64 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 677.48 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 680.80 | NIST | |
| Inp | 677.60 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 677.48 | NIST | |
| Tboil | [363.70; 364.87] | K |
|
| Tboil | 364.71 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 364.00 | K | NIST |
| Tboil | 363.90 | K | NIST |
| Tboil | 363.95 ± 0.30 | K | NIST |
| Tboil | Outlier 364.87 ± 0.02 | K | NIST |
| Tboil | 364.11 ± 0.50 | K | NIST |
| Tboil | 364.05 ± 0.20 | K | NIST |
| Tboil | 363.70 ± 0.40 | K | NIST |
| Tboil | 363.85 ± 0.60 | K | NIST |
| Tboil | 363.90 ± 0.50 | K | NIST |
| Tboil | 363.85 ± 0.50 | K | NIST |
| Tc | [550.93; 551.90] | K |
|
| Tc | 550.93 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 551.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 551.90 | K | NIST |
| Tfus | [134.55; 139.46] | K |
|
| Tfus | 139.45 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 139.35 ± 0.40 | K | NIST |
| Tfus | 139.40 ± 0.30 | K | NIST |
| Tfus | Outlier 134.55 ± 4.00 | K | NIST |
| Tfus | 139.44 ± 0.05 | K | NIST |
| Tfus | 139.46 ± 0.02 | K | NIST |
| Tfus | 139.39 ± 0.20 | K | NIST |
| Tfus | 139.46 ± 0.10 | K | NIST |
| Tfus | 139.39 ± 0.07 | K | NIST |
| Tfus | 139.44 ± 0.05 | K | NIST |
| Tfus | 139.44 ± 0.05 | K | NIST |
| Tfus | 139.44 ± 0.03 | K | NIST |
| Tfus | 136.40 ± 1.50 | K | NIST |
| Ttriple | [139.45; 139.48] | K |
|
| Ttriple | 139.45 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 139.48 ± 0.07 | K | NIST |
| UQi | 3.77 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.72 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.363 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| VCOSTALD | 0.38 | m3/kmol | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
| ωSRK | 0.28 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zc | 0.2770000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | [0.28; 0.28] |
|
|
| Zra | 0.28 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zra | 0.28 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [161.69; 226.12] | J/mol×K | [352.20; 500.20] |
|
| Cp,gas | 161.69 ± 0.32 | J/mol×K | 352.20 | NIST |
| Cp,gas | 172.23 ± 0.34 | J/mol×K | 375.20 | NIST |
| Cp,gas | 190.57 ± 0.38 | J/mol×K | 415.20 | NIST |
| Cp,gas | 207.77 ± 0.42 | J/mol×K | 455.20 | NIST |
| Cp,gas | 226.12 ± 0.45 | J/mol×K | 500.20 | NIST |
| ΔvapH | [30.40; 34.20] | kJ/mol | [322.62; 364.00] |
|
| ΔvapH | 32.83 ± 0.00 | kJ/mol | 322.62 | NIST |
| ΔvapH | 32.80 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 34.20 | kJ/mol | 330.50 | NIST |
| ΔvapH | 34.00 | kJ/mol | 332.50 | NIST |
| ΔvapH | 31.70 ± 0.10 | kJ/mol | 342.00 | NIST |
| ΔvapH | 30.40 | kJ/mol | 363.90 | NIST |
| ΔvapH | 30.40 ± 0.10 | kJ/mol | 364.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [99.53; 420.08] | J/mol×K | [200.00; 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 | 8.63180e+01 | |||
| Coefficient B | -8.31430e+02 | |||
| Coefficient C | 6.85024e+00 | |||
| Coefficient D | -5.97820e-04 | |||
| Coefficient E | 1.82760e-07 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 99.53 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 156.58 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 220.74 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 273.51 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 313.75 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 344.28 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 368.07 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 387.52 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 404.41 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 420.08 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [153.98; 218.35] | J/mol×K | [210.93; 363.92] |
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 | 6.57860e+01 | |||
| Coefficient B | -8.13450e+01 | |||
| Coefficient C | 4.23024e+00 | |||
| Coefficient D | 3.29310e-03 | |||
| Coefficient E | -1.34050e-06 | |||
| Temperature range, min. | 210.93 | |||
| Temperature range, max. | 363.92 | |||
| Cp,liquid | 153.98 | J/mol×K | 210.93 | Calculated Property |
| Cp,liquid | 160.83 | J/mol×K | 227.93 | Calculated Property |
| Cp,liquid | 167.72 | J/mol×K | 244.93 | Calculated Property |
| Cp,liquid | 174.67 | J/mol×K | 261.93 | Calculated Property |
| Cp,liquid | 181.70 | J/mol×K | 278.93 | Calculated Property |
| Cp,liquid | 188.82 | J/mol×K | 295.92 | Calculated Property |
| Cp,liquid | 196.04 | J/mol×K | 312.92 | Calculated Property |
| Cp,liquid | 203.37 | J/mol×K | 329.92 | Calculated Property |
| Cp,liquid | 210.81 | J/mol×K | 346.92 | Calculated Property |
| Cp,liquid | 218.35 | J/mol×K | 363.92 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0218006; 0.0001233] | Pa×s | [139.45; 508.65] |
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 | -1.13110e+01 | |||
| Coefficient B | 1.00060e+03 | |||
| Coefficient C | 6.35550e-02 | |||
| Coefficient D | -2.03880e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 508.65 | |||
| η | 0.0218006 | Pa×s | 139.45 | Calculated Property |
| η | 0.0043261 | Pa×s | 180.47 | Calculated Property |
| η | 0.0015643 | Pa×s | 221.49 | Calculated Property |
| η | 0.0007775 | Pa×s | 262.52 | Calculated Property |
| η | 0.0004666 | Pa×s | 303.54 | Calculated Property |
| η | 0.0003160 | Pa×s | 344.56 | Calculated Property |
| η | 0.0002322 | Pa×s | 385.58 | Calculated Property |
| η | 0.0001809 | Pa×s | 426.61 | Calculated Property |
| η | 0.0001470 | Pa×s | 467.63 | Calculated Property |
| η | 0.0001233 | Pa×s | 508.65 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [41.94; 0.00] | kJ/mol | [139.45; 551.00] |
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 | 5.96475e+01 | |||
| Coefficient B | 1.99220e+00 | |||
| Coefficient C | -3.90604e+00 | |||
| Coefficient D | 3.44234e+00 | |||
| Coefficient E | -1.06493e+00 | |||
| Critical temperature, Tc (K) | 5.51000e+02 | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 551.00 | |||
| ΔvapH | 41.94 | kJ/mol | 139.45 | Calculated Property |
| ΔvapH | 39.15 | kJ/mol | 185.18 | Calculated Property |
| ΔvapH | 36.96 | kJ/mol | 230.91 | Calculated Property |
| ΔvapH | 35.01 | kJ/mol | 276.63 | Calculated Property |
| ΔvapH | 33.03 | kJ/mol | 322.36 | Calculated Property |
| ΔvapH | 30.73 | kJ/mol | 368.09 | Calculated Property |
| ΔvapH | 27.80 | kJ/mol | 413.82 | Calculated Property |
| ΔvapH | 23.82 | kJ/mol | 459.54 | Calculated Property |
| ΔvapH | 17.89 | kJ/mol | 505.27 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 551.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [261.79; 389.38] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44248e+01 | |||
| Coefficient B | -3.27206e+03 | |||
| Coefficient C | -3.03370e+01 | |||
| Temperature range, min. | 261.79 | |||
| Temperature range, max. | 389.38 | |||
| Pvap | 1.33 | kPa | 261.79 | Calculated Property |
| Pvap | 3.02 | kPa | 275.97 | Calculated Property |
| Pvap | 6.24 | kPa | 290.14 | Calculated Property |
| Pvap | 11.97 | kPa | 304.32 | Calculated Property |
| Pvap | 21.54 | kPa | 318.50 | Calculated Property |
| Pvap | 36.68 | kPa | 332.67 | Calculated Property |
| Pvap | 59.56 | kPa | 346.85 | Calculated Property |
| Pvap | 92.77 | kPa | 361.03 | Calculated Property |
| Pvap | 139.34 | kPa | 375.20 | Calculated Property |
| Pvap | 202.66 | kPa | 389.38 | Calculated Property |
| Pvap | [2.86e-07; 3450.09] | kPa | [139.45; 551.00] |
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 | 5.23542e+01 | |||
| Coefficient B | -5.56130e+03 | |||
| Coefficient C | -5.59320e+00 | |||
| Coefficient D | 3.91240e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 551.00 | |||
| Pvap | 2.86e-07 | kPa | 139.45 | Calculated Property |
| Pvap | 1.17e-03 | kPa | 185.18 | Calculated Property |
| Pvap | 0.14 | kPa | 230.91 | Calculated Property |
| Pvap | 3.01 | kPa | 276.63 | Calculated Property |
| Pvap | 24.64 | kPa | 322.36 | Calculated Property |
| Pvap | 113.22 | kPa | 368.09 | Calculated Property |
| Pvap | 359.16 | kPa | 413.82 | Calculated Property |
| Pvap | 889.86 | kPa | 459.54 | Calculated Property |
| Pvap | 1859.99 | kPa | 505.27 | Calculated Property |
| Pvap | 3450.09 | kPa | 551.00 | Calculated Property |
| Pvap | [1.75e-07; 3508.11] | kPa | [139.45; 551.00] |
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 | 6.40317e+01 | |||
| Coefficient B | -6.01095e+03 | |||
| Coefficient C | -7.41243e+00 | |||
| Coefficient D | 6.01324e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 551.00 | |||
| Pvap | 1.75e-07 | kPa | 139.45 | Calculated Property |
| Pvap | 9.83e-04 | kPa | 185.18 | Calculated Property |
| Pvap | 0.13 | kPa | 230.91 | Calculated Property |
| Pvap | 2.96 | kPa | 276.63 | Calculated Property |
| Pvap | 24.49 | kPa | 322.36 | Calculated Property |
| Pvap | 112.30 | kPa | 368.09 | Calculated Property |
| Pvap | 355.22 | kPa | 413.82 | Calculated Property |
| Pvap | 881.27 | kPa | 459.54 | Calculated Property |
| Pvap | 1858.06 | kPa | 505.27 | Calculated Property |
| Pvap | 3508.11 | kPa | 551.00 | Calculated Property |
| Pvap | [9.02; 104.02] | kPa | [299.13; 365.78] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37411e+01 | |||
| Coefficient B | -2.86137e+03 | |||
| Coefficient C | -5.12220e+01 | |||
| Reference | Forziati, Norris, et al., 1949, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 299.13 | |||
| Temperature range, max. | 365.78 | |||
| Pvap | 9.02 | kPa | 299.13 | Calculated Property |
| Pvap | 12.60 | kPa | 306.54 | Calculated Property |
| Pvap | 17.28 | kPa | 313.94 | Calculated Property |
| Pvap | 23.30 | kPa | 321.35 | Calculated Property |
| Pvap | 30.91 | kPa | 328.75 | Calculated Property |
| Pvap | 40.40 | kPa | 336.16 | Calculated Property |
| Pvap | 52.11 | kPa | 343.56 | Calculated Property |
| Pvap | 66.36 | kPa | 350.97 | Calculated Property |
| Pvap | 83.54 | kPa | 358.37 | Calculated Property |
| Pvap | 104.02 | kPa | 365.78 | Calculated Property |
| Pvap | [9.02; 104.02] | kPa | [299.13; 365.78] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37411e+01 | |||
| Coefficient B | -2.86137e+03 | |||
| Coefficient C | -5.12220e+01 | |||
| Reference | Forziati, Norris, et al., 1949 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 299.13 | |||
| Temperature range, max. | 365.78 | |||
| Pvap | 9.02 | kPa | 299.13 | Calculated Property |
| Pvap | 12.60 | kPa | 306.54 | Calculated Property |
| Pvap | 17.28 | kPa | 313.94 | Calculated Property |
| Pvap | 23.30 | kPa | 321.35 | Calculated Property |
| Pvap | 30.91 | kPa | 328.75 | Calculated Property |
| Pvap | 40.40 | kPa | 336.16 | Calculated Property |
| Pvap | 52.11 | kPa | 343.56 | Calculated Property |
| Pvap | 66.36 | kPa | 350.97 | Calculated Property |
| Pvap | 83.54 | kPa | 358.37 | Calculated Property |
| Pvap | 104.02 | kPa | 365.78 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [873.90; 272.18] | kg/m3 | [139.45; 551.00] |
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 | 7.58232e+01 | |||
| Coefficient B | 2.78580e-01 | |||
| Coefficient C | 5.51000e+02 | |||
| Coefficient D | 3.12930e-01 | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 551.00 | |||
| ρl | 873.90 | kg/m3 | 139.45 | Calculated Property |
| ρl | 837.78 | kg/m3 | 185.18 | Calculated Property |
| ρl | 800.11 | kg/m3 | 230.91 | Calculated Property |
| ρl | 760.49 | kg/m3 | 276.63 | Calculated Property |
| ρl | 718.37 | kg/m3 | 322.36 | Calculated Property |
| ρl | 672.85 | kg/m3 | 368.09 | Calculated Property |
| ρl | 622.41 | kg/m3 | 413.82 | Calculated Property |
| ρl | 563.99 | kg/m3 | 459.54 | Calculated Property |
| ρl | 489.30 | kg/m3 | 505.27 | Calculated Property |
| ρl | 272.18 | kg/m3 | 551.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 1.45e-05] | N/m | [139.45; 544.42] |
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 | -9.57940e-03 | |||
| Coefficient B | 2.90180e+01 | |||
| Coefficient C | -3.10510e+00 | |||
| Coefficient D | -4.94830e-05 | |||
| Coefficient E | -5.29000e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 551 K. | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 544.42 | |||
| γ | 0.04 | N/m | 139.45 | Calculated Property |
| γ | 0.03 | N/m | 184.45 | Calculated Property |
| γ | 0.03 | N/m | 229.44 | Calculated Property |
| γ | 0.02 | N/m | 274.44 | Calculated Property |
| γ | 0.02 | N/m | 319.43 | Calculated Property |
| γ | 0.01 | N/m | 364.43 | Calculated Property |
| γ | 0.01 | N/m | 409.43 | Calculated Property |
| γ | 0.01 | N/m | 454.42 | Calculated Property |
| γ | 0.00 | N/m | 499.42 | Calculated Property |
| γ | 1.45e-05 | N/m | 544.42 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.10] | W/m×K | [139.45; 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 | 2.17210e-03 | |||
| Coefficient B | 6.28820e-01 | |||
| Coefficient C | 2.03610e+02 | |||
| Coefficient D | 4.46440e+05 | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 139.45 | Calculated Property |
| λgas | 0.01 | W/m×K | 235.07 | Calculated Property |
| λgas | 0.01 | W/m×K | 330.68 | Calculated Property |
| λgas | 0.02 | W/m×K | 426.30 | Calculated Property |
| λgas | 0.04 | W/m×K | 521.92 | Calculated Property |
| λgas | 0.05 | W/m×K | 617.53 | Calculated Property |
| λgas | 0.06 | W/m×K | 713.15 | Calculated Property |
| λgas | 0.08 | W/m×K | 808.77 | Calculated Property |
| λgas | 0.09 | W/m×K | 904.38 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.10] | W/m×K | [139.45; 363.92] |
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 | -4.17320e-02 | |||
| Coefficient B | 3.59950e+00 | |||
| Coefficient C | -1.58100e+00 | |||
| Coefficient D | -4.89110e-04 | |||
| Coefficient E | -1.64760e-06 | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 363.92 | |||
| λliquid | 0.15 | W/m×K | 139.45 | Calculated Property |
| λliquid | 0.14 | W/m×K | 164.39 | Calculated Property |
| λliquid | 0.14 | W/m×K | 189.33 | Calculated Property |
| λliquid | 0.13 | W/m×K | 214.27 | Calculated Property |
| λliquid | 0.13 | W/m×K | 239.21 | Calculated Property |
| λliquid | 0.12 | W/m×K | 264.16 | Calculated Property |
| λliquid | 0.12 | W/m×K | 289.10 | Calculated Property |
| λliquid | 0.11 | W/m×K | 314.04 | Calculated Property |
| λliquid | 0.10 | W/m×K | 338.98 | Calculated Property |
| λliquid | 0.10 | W/m×K | 363.92 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclopentane, 1,3-dimethyl-, cis-.
Sources
- KDB Vapor Pressure Data
- 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.
- Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
- 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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