Chemical Properties of Cyclopentane, propyl- (CAS 2040-96-2)

Cyclopentane, propyl-

InChI
InChI=1S/C8H16/c1-2-5-8-6-3-4-7-8/h8H,2-7H2,1H3
InChI Key
KDIAMAVWIJYWHN-UHFFFAOYSA-N
Formula
C8H16
SMILES
CCCC1CCCC1
Molecular Weight1
112.21
CAS
2040-96-2
Other Names
  • 1-Cyclopentylpropane
  • Cyclopentane, n-propyl-
  • Propylcyclopentane
  • n-Propylcyclopentane
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Physical Properties

Property Value Unit Source
ω [0.3266; 0.3350]   Show Hide
ω 0.3350 Passut and Danner (1973), critical constants and acentric factors Compiled value
ω 0.3266 ChemSep v8.3 pure component data Compiled value
ω 0.3350 KDB
AP 317.650 K KDB
ΔcH°liquid [-5245.98; -5245.60] kJ/mol Show Hide
ΔcH°liquid -5245.98 ± 0.75 kJ/mol NIST
ΔcH°liquid -5245.60 ± 1.20 kJ/mol NIST
μ 0.00 debye ChemSep v8.3 pure component data Compiled value
ΔfG° [52.63; 53.44] kJ/mol Show Hide
ΔfG° 53.44 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° 52.63 kJ/mol KDB
Δc,grossH 5245.65 kJ/mol KDB
Δc,netH 4893.565 kJ/mol KDB
ΔfH°gas [-148.20; -147.60] kJ/mol Show Hide
ΔfH°gas -148.10 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -148.20 kJ/mol KDB
ΔfH°gas -147.60 kJ/mol NIST
ΔfH°gas -148.10 ± 1.30 kJ/mol NIST
ΔfH°liquid [-189.20; -188.70] kJ/mol Show Hide
ΔfH°liquid -188.70 ± 0.92 kJ/mol NIST
ΔfH°liquid -189.20 ± 1.30 kJ/mol NIST
ΔfusH° 10.41 kJ/mol Joback Calculated Property
ΔvapH° [41.08; 41.12] kJ/mol Show Hide
ΔvapH° 41.12 kJ/mol NIST
ΔvapH° 41.10 kJ/mol NIST
ΔvapH° 41.10 ± 0.10 kJ/mol NIST
ΔvapH° 41.08 kJ/mol NIST
ΔvapH° 41.10 kJ/mol NIST
IE [9.34; 10.00] eV Show Hide
IE 9.34 ± 0.05 eV NIST
IE 10.00 ± 0.04 eV NIST
log10WS [-4.74; -4.74]   Show Hide
log10WS -4.74 Aq. Solubility Prediction
log10WS -4.74 Estimated Solubility
logPoct/wat 2.977 Crippen Calculated Property
McVol 112.720 ml/mol McGowan Calculated Property
Pc [2999.22; 3020.00] kPa Show Hide
Pc 2999.22 kPa Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc 3020.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 3000.00 kPa KDB
Ptriple 4.59e-08 kPa ChemSep v8.3 pure component data Compiled value
Inp [808.20; 857.00]   Show Hide
Inp 826.00 NIST
Inp 827.20 NIST
Inp 831.60 NIST
Inp 829.40 NIST
Inp 833.40 NIST
Inp 829.90 NIST
Inp 839.20 NIST
Inp 830.10 NIST
Inp 830.40 NIST
Inp 833.80 NIST
Inp 837.10 NIST
Inp 837.30 NIST
Inp 839.00 NIST
Inp 840.00 NIST
Inp 832.00 NIST
Inp 836.00 NIST
Inp 848.00 NIST
Inp Outlier 851.00 NIST
Inp Outlier 853.00 NIST
Inp Outlier 857.00 NIST
Inp 830.00 NIST
Inp 834.00 NIST
Inp 848.00 NIST
Inp Outlier 849.00 NIST
Inp 830.00 NIST
Inp 833.00 NIST
Inp 834.00 NIST
Inp 836.00 NIST
Inp 839.00 NIST
Inp 830.30 NIST
Inp 830.00 NIST
Inp Outlier 851.00 NIST
Inp 826.00 NIST
Inp 830.00 NIST
Inp 834.00 NIST
Inp 838.00 NIST
Inp 834.00 NIST
Inp 834.00 NIST
Inp 845.00 NIST
Inp Outlier 808.20 NIST
Inp 841.73 NIST
Inp 832.00 NIST
Inp 831.30 NIST
Inp 836.50 NIST
Inp 832.70 NIST
Inp 827.12 NIST
Inp 827.00 NIST
Inp 830.60 NIST
Inp 825.30 NIST
Inp 825.60 NIST
Inp 834.00 NIST
Inp 830.00 NIST
Inp 839.00 NIST
Inp 828.00 NIST
Inp 834.00 NIST
Inp 828.00 NIST
Inp 831.00 NIST
Inp 832.00 NIST
Inp 830.00 NIST
Inp 833.00 NIST
Inp 832.00 NIST
Inp 830.70 NIST
Inp 832.30 NIST
Inp 834.50 NIST
Inp 836.20 NIST
Inp 837.60 NIST
Inp 838.80 NIST
Inp 830.00 NIST
Inp 832.00 NIST
Inp 834.00 NIST
Inp 836.00 NIST
Inp 837.00 NIST
Inp 838.00 NIST
Inp Outlier 817.00 NIST
Inp 826.00 NIST
Inp 830.00 NIST
Inp 832.00 NIST
Inp 832.30 NIST
Inp 830.00 NIST
Inp 838.00 NIST
Inp 827.00 NIST
Inp 834.00 NIST
Ip [890.60; 912.00]   Show Hide
Ip 912.00 NIST
Ip 895.00 NIST
Ip 900.00 NIST
Ip 904.00 NIST
Ip 898.00 NIST
Ip 903.00 NIST
Ip 907.00 NIST
Ip 891.00 NIST
Ip 894.00 NIST
Ip 898.00 NIST
Ip 903.00 NIST
Ip 907.10 NIST
Ip 890.60 NIST
Ip 894.00 NIST
Ip 912.00 NIST
Ip 912.00 NIST
Ip 903.00 NIST
S°gas 414.47 J/mol×K NIST
S°liquid 310.83 J/mol×K NIST
Tboil [403.80; 454.60] K Show Hide
Tboil 404.11 K ChemSep v8.3 pure component data Compiled value
Tboil 404.10 K KDB
Tboil 404.20 K NIST
Tboil 404.10 K NIST
Tboil 404.10 ± 0.30 K NIST
Tboil 404.10 ± 0.30 K NIST
Tboil Outlier 454.60 ± 0.80 K NIST
Tboil 404.10 ± 0.30 K NIST
Tboil 404.10 ± 0.30 K NIST
Tboil 404.07 ± 0.30 K NIST
Tboil 404.20 ± 0.50 K NIST
Tboil 404.09 ± 0.02 K NIST
Tboil 404.15 ± 0.40 K NIST
Tboil 404.07 ± 0.30 K NIST
Tboil 404.08 ± 0.15 K NIST
Tboil 403.96 ± 0.20 K NIST
Tboil 404.00 ± 0.30 K NIST
Tboil 403.96 ± 0.20 K NIST
Tboil 404.05 ± 0.30 K NIST
Tboil 404.07 ± 0.30 K NIST
Tboil 403.95 ± 0.40 K NIST
Tboil 403.85 ± 0.50 K NIST
Tboil 404.50 ± 0.60 K NIST
Tboil 403.80 ± 0.50 K NIST
Tboil 404.45 ± 0.60 K NIST
Tboil 404.55 ± 0.60 K NIST
Tc [596.00; 603.15] K Show Hide
Tc 603.15 K Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc 596.00 K ChemSep v8.3 pure component data Compiled value
Tc 603.00 K KDB
Tfus [151.50; 156.00] K Show Hide
Tfus 156.00 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 155.81 K ChemSep v8.3 pure component data Compiled value
Tfus 155.80 K KDB
Tfus 156.00 K Aq. Solubility Prediction
Tfus 155.63 ± 0.50 K NIST
Tfus 155.81 ± 0.04 K NIST
Tfus 155.63 ± 0.20 K NIST
Tfus 155.74 ± 0.01 K NIST
Tfus 153.83 ± 1.50 K NIST
Tfus 155.23 ± 0.10 K NIST
Tfus 154.50 ± 2.00 K NIST
Tfus 155.63 ± 0.50 K NIST
Tfus 155.85 ± 0.30 K NIST
Tfus Outlier 151.50 ± 0.40 K NIST
Ttriple [155.79; 155.81] K Show Hide
Ttriple 155.81 K ChemSep v8.3 pure component data Compiled value
Ttriple 155.79 ± 0.01 K NIST
Ttriple 155.80 ± 0.60 K NIST
Ttriple 155.79 ± 0.01 K NIST
UQi 4.32 ChemSep v8.3 pure component data Compiled value
URi 5.39 ChemSep v8.3 pure component data Compiled value
Vc [0.425; 0.428] m3/kmol Show Hide
Vc 0.428 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.425 m3/kmol KDB
Zc [0.2543060; 0.2610000]   Show Hide
Zc 0.2610000 ChemSep v8.3 pure component data Compiled value
Zc 0.2543060 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid 216.27 J/mol×K 298.15 NIST
Csat [173.70; 251.10] J/mol×K [160.00; 370.00] Show Hide
Csat 173.70 J/mol×K 160.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 174.90 J/mol×K 170.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 176.50 J/mol×K 180.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 178.50 J/mol×K 190.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 180.70 J/mol×K 200.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 183.30 J/mol×K 210.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 186.10 J/mol×K 220.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 189.20 J/mol×K 230.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 192.60 J/mol×K 240.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 196.20 J/mol×K 250.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 200.00 J/mol×K 260.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 204.00 J/mol×K 270.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 205.30 J/mol×K 273.15 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 208.20 J/mol×K 280.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 212.60 J/mol×K 290.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 216.20 J/mol×K 298.15 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 217.10 J/mol×K 300.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 221.70 J/mol×K 310.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 226.40 J/mol×K 320.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 231.30 J/mol×K 330.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 236.10 J/mol×K 340.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 241.10 J/mol×K 350.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 246.10 J/mol×K 360.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 251.10 J/mol×K 370.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH [10.03; 10.04] kJ/mol [155.79; 155.80] Show Hide
ΔfusH 10.03 kJ/mol 155.79 NIST
ΔfusH 10.03 kJ/mol 155.79 NIST
ΔfusH 10.04 kJ/mol 155.80 NIST
ΔfusH 10.04 kJ/mol 155.80 NIST
ΔvapH [34.11; 39.20] kJ/mol [364.50; 404.10] Show Hide
ΔvapH 39.20 kJ/mol 364.50 NIST
ΔvapH 34.11 kJ/mol 404.10 KDB
ΔvapH 34.70 kJ/mol 404.10 NIST
n0 1.42389 298.15 KDB
ρl 781.00 kg/m3 289.00 KDB
ΔfusS [64.44; 64.44] J/mol×K [155.79; 155.79] Show Hide
ΔfusS 64.44 J/mol×K 155.79 NIST
ΔfusS 64.44 J/mol×K 155.79 NIST
γ 0.02 N/m 293.20 KDB

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [106.65; 475.68] J/mol×K [200.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A8.23870e+01
Coefficient B-6.76010e+02
Coefficient C6.60624e+00
Coefficient D-1.95460e-04
Coefficient E4.98540e-08
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 106.65 J/mol×K 200.00 Calculated Property
Cp,gas 180.12 J/mol×K 344.44 Calculated Property
Cp,gas 253.08 J/mol×K 488.89 Calculated Property
Cp,gas 311.70 J/mol×K 633.33 Calculated Property
Cp,gas 356.96 J/mol×K 777.78 Calculated Property
Cp,gas 392.01 J/mol×K 922.22 Calculated Property
Cp,gas 419.60 J/mol×K 1066.67 Calculated Property
Cp,gas 441.80 J/mol×K 1211.11 Calculated Property
Cp,gas 460.12 J/mol×K 1355.56 Calculated Property
Cp,gas 475.68 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [173.67; 265.07] J/mol×K [155.81; 404.11] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.21270e+02
Coefficient B2.81760e+02
Coefficient C-1.92655e-01
Coefficient D1.75450e-02
Coefficient E-1.60820e-05
Temperature range, min.155.81
Temperature range, max.404.11
Cp,liquid 173.67 J/mol×K 155.81 Calculated Property
Cp,liquid 177.00 J/mol×K 183.40 Calculated Property
Cp,liquid 183.36 J/mol×K 210.99 Calculated Property
Cp,liquid 192.00 J/mol×K 238.58 Calculated Property
Cp,liquid 202.44 J/mol×K 266.17 Calculated Property
Cp,liquid 214.28 J/mol×K 293.75 Calculated Property
Cp,liquid 227.06 J/mol×K 321.34 Calculated Property
Cp,liquid 240.23 J/mol×K 348.93 Calculated Property
Cp,liquid 253.14 J/mol×K 376.52 Calculated Property
Cp,liquid 265.07 J/mol×K 404.11 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0043904; 0.0002710] Pa×s [200.00; 404.11] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-2.27250e+01
Coefficient B1.60180e+03
Coefficient C1.75120e+00
Coefficient D2.31080e-07
Coefficient E2.00000e+00
Temperature range, min.200.00
Temperature range, max.404.11
η 0.0043904 Pa×s 200.00 Calculated Property
η 0.0023491 Pa×s 222.68 Calculated Property
η 0.0014354 Pa×s 245.36 Calculated Property
η 0.0009671 Pa×s 268.04 Calculated Property
η 0.0007016 Pa×s 290.72 Calculated Property
η 0.0005388 Pa×s 313.39 Calculated Property
η 0.0004327 Pa×s 336.07 Calculated Property
η 0.0003603 Pa×s 358.75 Calculated Property
η 0.0003088 Pa×s 381.43 Calculated Property
η 0.0002710 Pa×s 404.11 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [51.51; 15.68] kJ/mol [155.81; 572.83] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A7.08810e+01
Coefficient B1.47769e+00
Coefficient C-1.91931e+00
Coefficient D1.21986e+00
Coefficient E-3.32624e-01
Critical temperature, Tc (K)5.96000e+02
Temperature range, min.155.81
Temperature range, max.572.83
ΔvapH 51.51 kJ/mol 155.81 Calculated Property
ΔvapH 47.74 kJ/mol 202.15 Calculated Property
ΔvapH 44.44 kJ/mol 248.48 Calculated Property
ΔvapH 41.44 kJ/mol 294.82 Calculated Property
ΔvapH 38.57 kJ/mol 341.15 Calculated Property
ΔvapH 35.66 kJ/mol 387.49 Calculated Property
ΔvapH 32.52 kJ/mol 433.82 Calculated Property
ΔvapH 28.83 kJ/mol 480.16 Calculated Property
ΔvapH 23.95 kJ/mol 526.49 Calculated Property
ΔvapH 15.68 kJ/mol 572.83 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [291.64; 432.35] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.41315e+01
Coefficient B-3.42008e+03
Coefficient C-4.45910e+01
Temperature range, min.291.64
Temperature range, max.432.35
Pvap 1.33 kPa 291.64 Calculated Property
Pvap 3.04 kPa 307.27 Calculated Property
Pvap 6.32 kPa 322.91 Calculated Property
Pvap 12.14 kPa 338.54 Calculated Property
Pvap 21.85 kPa 354.18 Calculated Property
Pvap 37.16 kPa 369.81 Calculated Property
Pvap 60.20 kPa 385.45 Calculated Property
Pvap 93.48 kPa 401.08 Calculated Property
Pvap 139.89 kPa 416.72 Calculated Property
Pvap 202.64 kPa 432.35 Calculated Property
Pvap [4.49e-08; 3063.03] kPa [155.81; 596.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A8.84874e+01
Coefficient B-7.84654e+03
Coefficient C-1.09384e+01
Coefficient D7.33203e-06
Coefficient E2.00000e+00
Temperature range, min.155.81
Temperature range, max.596.00
Pvap 4.49e-08 kPa 155.81 Calculated Property
Pvap 4.33e-04 kPa 204.72 Calculated Property
Pvap 0.08 kPa 253.63 Calculated Property
Pvap 2.10 kPa 302.54 Calculated Property
Pvap 19.01 kPa 351.45 Calculated Property
Pvap 91.53 kPa 400.36 Calculated Property
Pvap 297.16 kPa 449.27 Calculated Property
Pvap 748.71 kPa 498.18 Calculated Property
Pvap 1598.60 kPa 547.09 Calculated Property
Pvap 3063.03 kPa 596.00 Calculated Property
Pvap [6.03e-08; 2951.13] kPa [155.81; 603.00] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A7.66656e+01
Coefficient B-7.41133e+03
Coefficient C-9.07967e+00
Coefficient D4.79197e-06
Coefficient E0.00000e+00
Temperature range, min.155.81
Temperature range, max.603.00
Pvap 6.03e-08 kPa 155.81 Calculated Property
Pvap 5.26e-04 kPa 205.50 Calculated Property
Pvap 0.09 kPa 255.19 Calculated Property
Pvap 2.38 kPa 304.87 Calculated Property
Pvap 21.32 kPa 354.56 Calculated Property
Pvap 101.36 kPa 404.25 Calculated Property
Pvap 322.85 kPa 453.94 Calculated Property
Pvap 790.66 kPa 503.62 Calculated Property
Pvap 1622.48 kPa 553.31 Calculated Property
Pvap 2951.13 kPa 603.00 Calculated Property
Pvap [6.39; 104.01] kPa [325.02; 405.07] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.39171e+01
Coefficient B-3.20970e+03
Coefficient C-5.89220e+01
ReferenceForziati, Norris, et al., 1949
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.325.02
Temperature range, max.405.07
Pvap 6.39 kPa 325.02 Calculated Property
Pvap 9.44 kPa 333.91 Calculated Property
Pvap 13.61 kPa 342.81 Calculated Property
Pvap 19.19 kPa 351.70 Calculated Property
Pvap 26.51 kPa 360.60 Calculated Property
Pvap 35.95 kPa 369.49 Calculated Property
Pvap 47.94 kPa 378.39 Calculated Property
Pvap 62.94 kPa 387.28 Calculated Property
Pvap 81.45 kPa 396.18 Calculated Property
Pvap 104.01 kPa 405.07 Calculated Property
Property Value Unit Temperature (K) Source
ρl [876.17; 444.36] kg/m3 [155.81; 572.83] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A7.07624e+01
Coefficient B2.69340e-01
Coefficient C5.96000e+02
Coefficient D2.81690e-01
Temperature range, min.155.81
Temperature range, max.572.83
ρl 876.17 kg/m3 155.81 Calculated Property
ρl 844.22 kg/m3 202.15 Calculated Property
ρl 810.76 kg/m3 248.48 Calculated Property
ρl 775.45 kg/m3 294.82 Calculated Property
ρl 737.82 kg/m3 341.15 Calculated Property
ρl 697.11 kg/m3 387.49 Calculated Property
ρl 652.14 kg/m3 433.82 Calculated Property
ρl 600.67 kg/m3 480.16 Calculated Property
ρl 537.66 kg/m3 526.49 Calculated Property
ρl 444.36 kg/m3 572.83 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.00] N/m [155.81; 572.83] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-1.48460e-02
Coefficient B1.56190e+01
Coefficient C-2.86810e+00
Coefficient D-4.82410e-04
Coefficient E-3.12040e-06
Temperature range, min.155.81
Temperature range, max.572.83
γ 0.04 N/m 155.81 Calculated Property
γ 0.03 N/m 202.15 Calculated Property
γ 0.03 N/m 248.48 Calculated Property
γ 0.02 N/m 294.82 Calculated Property
γ 0.02 N/m 341.15 Calculated Property
γ 0.02 N/m 387.49 Calculated Property
γ 0.01 N/m 433.82 Calculated Property
γ 0.01 N/m 480.16 Calculated Property
γ 0.00 N/m 526.49 Calculated Property
γ 0.00 N/m 572.83 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.09] W/m×K [155.81; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A9.83090e-05
Coefficient B1.06360e+00
Coefficient C6.11410e+02
Coefficient D3.31750e+04
Temperature range, min.155.81
Temperature range, max.1000.00
λgas 0.00 W/m×K 155.81 Calculated Property
λgas 0.01 W/m×K 249.61 Calculated Property
λgas 0.02 W/m×K 343.41 Calculated Property
λgas 0.02 W/m×K 437.21 Calculated Property
λgas 0.03 W/m×K 531.01 Calculated Property
λgas 0.04 W/m×K 624.80 Calculated Property
λgas 0.06 W/m×K 718.60 Calculated Property
λgas 0.07 W/m×K 812.40 Calculated Property
λgas 0.08 W/m×K 906.20 Calculated Property
λgas 0.09 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.14; 0.09] W/m×K [155.81; 404.11] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A-3.37410e-02
Coefficient B2.53080e+00
Coefficient C-1.62370e+00
Coefficient D-5.81860e-04
Coefficient E-1.31180e-06
Temperature range, min.155.81
Temperature range, max.404.11
λliquid 0.14 W/m×K 155.81 Calculated Property
λliquid 0.14 W/m×K 183.40 Calculated Property
λliquid 0.13 W/m×K 210.99 Calculated Property
λliquid 0.13 W/m×K 238.58 Calculated Property
λliquid 0.12 W/m×K 266.17 Calculated Property
λliquid 0.12 W/m×K 293.75 Calculated Property
λliquid 0.11 W/m×K 321.34 Calculated Property
λliquid 0.10 W/m×K 348.93 Calculated Property
λliquid 0.10 W/m×K 376.52 Calculated Property
λliquid 0.09 W/m×K 404.11 Calculated Property

Similar Compounds

Cyclopentane, butyl-. Cyclopentane, ethyl-. Cyclopentane, heptyl-. Cyclopentane, hexyl-. n-Pentadecylcyclopentane. Cyclopentane, (4-octyldodecyl)-. Cyclopentane, tetradecyl-. Cyclopentane, nonyl-. n-Heptadecyl-cyclopentane. Cyclopentane, octadecyl-. n-Dodecylcyclopentane. Tridecylcyclopentane. Cyclopentane, undecyl-. 1-cyclopentylicosane. Cyclopentane, hexadecyl-.

Find more compounds similar to Cyclopentane, propyl-.

Sources

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.