Chemical Properties of 2,3-Pentadiene (CAS 591-96-8)

2,3-Pentadiene

InChI
InChI=1S/C5H8/c1-3-5-4-2/h3-4H,1-2H3
InChI Key
PODAMDNJNMAKAZ-UHFFFAOYSA-N
Formula
C5H8
SMILES
CC=C=CC
Molecular Weight1
68.12
CAS
591-96-8
Other Names
  • 1,3-Dimethylallene
  • CH3CH=C=CHCH3
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Physical Properties

Property Value Unit Source
ω 0.2040 KDB
ΔcH°gas -3243.90 ± 0.67 kJ/mol NIST
ΔfG° 199.72 kJ/mol Joback Calculated Property
Δc,grossH 3214.27 kJ/mol KDB
Δc,netH 3038.253 kJ/mol KDB
ΔfH°gas 133.00 ± 0.71 kJ/mol NIST
ΔfusH° 11.04 kJ/mol Joback Calculated Property
ΔvapH° 29.50 kJ/mol NIST
IE [9.13; 9.26] eV Show Hide
IE 9.13 ± 0.02 eV NIST
IE 9.26 eV NIST
IE 9.13 eV NIST
logPoct/wat 1.737 Crippen Calculated Property
McVol 72.710 ml/mol McGowan Calculated Property
Pc 4140.00 kPa KDB
Inp [530.00; 556.00]   Show Hide
Inp 531.00 NIST
Inp 530.00 NIST
Inp 530.00 NIST
Inp 531.10 NIST
Inp 530.00 NIST
Inp 530.00 NIST
Inp 532.00 NIST
Inp 531.00 NIST
Inp 531.00 NIST
Inp 530.00 NIST
Inp 539.00 NIST
Inp 544.00 NIST
Inp Outlier 556.00 NIST
Inp 531.00 NIST
Inp 530.00 NIST
Inp 539.00 NIST
Inp 544.00 NIST
Inp Outlier 556.00 NIST
S°gas 329.11 J/mol×K NIST
S°liquid 237.32 J/mol×K NIST
Tboil [321.35; 321.40] K Show Hide
Tboil 321.40 K KDB
Tboil 321.35 ± 0.40 K NIST
Tc 505.80 K KDB
Tfus [147.43; 148.00] K Show Hide
Tfus 147.55 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus Outlier 148.00 K KDB
Tfus 147.43 ± 0.06 K NIST
Tfus 147.43 ± 0.20 K NIST
Tfus 147.46 ± 0.05 K NIST
Tfus 147.47 ± 0.04 K NIST
Tfus 147.50 ± 0.02 K NIST
Ttriple [147.52; 147.52] K Show Hide
Ttriple 147.52 ± 0.05 K NIST
Ttriple 147.52 ± 0.05 K NIST
Vc 0.276 m3/kmol KDB
Zc 0.2712100 KDB

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid 152.34 J/mol×K 298.15 NIST
Csat [135.90; 157.40] J/mol×K [150.00; 320.00] Show Hide
Csat 135.90 J/mol×K 150.00 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 135.90 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 136.10 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 136.40 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 136.90 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 137.60 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 138.40 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 139.40 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 140.60 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 141.90 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 143.40 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 145.00 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 146.70 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 147.30 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 148.60 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 150.60 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 152.40 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 152.80 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 155.00 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 157.40 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
ΔfusH [6.13; 6.13] kJ/mol [147.50; 147.52] Show Hide
ΔfusH 6.13 kJ/mol 147.50 NIST
ΔfusH 6.13 kJ/mol 147.50 NIST
ΔfusH 6.13 kJ/mol 147.52 NIST
ΔfusH 6.13 kJ/mol 147.52 NIST
ΔvapH [28.24; 33.20] kJ/mol [230.00; 321.40] Show Hide
ΔvapH 33.20 kJ/mol 230.00 NIST
ΔvapH 32.30 kJ/mol 246.00 NIST
ΔvapH 31.10 kJ/mol 294.00 NIST
ΔvapH 29.60 kJ/mol 310.00 NIST
ΔvapH 28.24 kJ/mol 321.40 KDB
n0 1.42509 298.15 KDB
ΔfusS [44.93; 44.93] J/mol×K [147.52; 147.52] Show Hide
ΔfusS 44.93 J/mol×K 147.52 NIST
ΔfusS 44.93 J/mol×K 147.52 NIST

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [95.03; 217.61] J/mol×K [273.00; 1000.00] Joback Predicted correlation Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is Cp,gas in J/mol×K, T in K
Coefficient A1.24700e+01
Coefficient B3.48140e-01
Coefficient C-1.76600e-04
Coefficient D3.36000e-08
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 95.03 J/mol×K 273.00 Calculated Property
Cp,gas 115.02 J/mol×K 353.78 Calculated Property
Cp,gas 133.16 J/mol×K 434.56 Calculated Property
Cp,gas 149.58 J/mol×K 515.33 Calculated Property
Cp,gas 164.36 J/mol×K 596.11 Calculated Property
Cp,gas 177.63 J/mol×K 676.89 Calculated Property
Cp,gas 189.48 J/mol×K 757.67 Calculated Property
Cp,gas 200.02 J/mol×K 838.44 Calculated Property
Cp,gas 209.36 J/mol×K 919.22 Calculated Property
Cp,gas 217.61 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.62] kPa [232.42; 343.71] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.41058e+01
Coefficient B-2.69205e+03
Coefficient C-3.76010e+01
Temperature range, min.232.42
Temperature range, max.343.71
Pvap 1.33 kPa 232.42 Calculated Property
Pvap 3.04 kPa 244.79 Calculated Property
Pvap 6.32 kPa 257.15 Calculated Property
Pvap 12.16 kPa 269.52 Calculated Property
Pvap 21.88 kPa 281.88 Calculated Property
Pvap 37.20 kPa 294.25 Calculated Property
Pvap 60.26 kPa 306.61 Calculated Property
Pvap 93.54 kPa 318.98 Calculated Property
Pvap 139.93 kPa 331.34 Calculated Property
Pvap 202.62 kPa 343.71 Calculated Property
Pvap [0.25; 3.20] kPa [213.14; 247.10] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.47084e+01
Coefficient B-2.89245e+03
Coefficient C-3.35850e+01
ReferenceOsborn and Douslin, 1969
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.213.14
Temperature range, max.247.10
Pvap 0.25 kPa 213.14 Calculated Property
Pvap 0.34 kPa 216.91 Calculated Property
Pvap 0.47 kPa 220.69 Calculated Property
Pvap 0.64 kPa 224.46 Calculated Property
Pvap 0.86 kPa 228.23 Calculated Property
Pvap 1.14 kPa 232.01 Calculated Property
Pvap 1.50 kPa 235.78 Calculated Property
Pvap 1.94 kPa 239.55 Calculated Property
Pvap 2.50 kPa 243.33 Calculated Property
Pvap 3.20 kPa 247.10 Calculated Property

Similar Compounds

1,2-Butadiene. 2-METHYL-2,3-PENTADIENE. 2,3-Hexadiene. 3,4-Heptadiene. 1,2-Pentadiene. 2,3-Hexadiene, 2-methyl-. Propene. Propene-d6. 2,3-Pentadiene, 2,4-dimethyl-. 1,1-Dibromo-1-propene. 1,2-Butadiene, 3-methyl-. 1-Propene, 1,1-dichloro-. 3,4-Pentadienal. 2,3-Butadien-1-ol. Propene, 1,1-difluoro-.

Find more compounds similar to 2,3-Pentadiene.

Sources

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