Chemical Properties of DIISOPROPYL SUCCINATE

DIISOPROPYL SUCCINATE

InChI
InChI=1S/C10H18O4/c1-7(2)13-9(11)5-6-10(12)14-8(3)4/h7-8H,5-6H2,1-4H3
InChI Key
YPLYFEUBZLLLIY-UHFFFAOYSA-N
Formula
C10H18O4
SMILES
CC(C)OC(=O)CCC(=O)OC(C)C
Molecular Weight1
202.25
Other Names
  • Diisopropyl butanedioate
  • bis(1-methylethyl) butanedioate
  • butanedioic acid, bis(1-methylethyl) ester
  • succinic acid, diisopropyl ester
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
ΔfH°gas -912.02 kJ/mol Relay (1.0) Calculated Property
ΔfusH° [64.48; 67.60] kJ/mol Show Hide
ΔfusH° 67.60 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 67.28 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 66.95 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 66.63 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 66.31 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 66.08 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 65.77 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 65.55 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 65.23 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 65.00 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 64.69 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔfusH° 64.48 kJ/mol Vapour pressure and enthalpy of vaporization of di-iso-propyl and di-tert-butyl esters of dicarboxylic acids
ΔvapH° 64.71 kJ/mol Relay (1.0) Calculated Property
IE 9.77 eV Relay (1.0) Calculated Property
log10WS -2.07 Relay (1.0) Calculated Property
logPoct/wat 1.670 Crippen Calculated Property
McVol 166.640 ml/mol McGowan Calculated Property
Pc 2159.31 kPa Joback Calculated Property
Inp [1220.00; 1226.00]   Show Hide
Inp 1226.00 NIST
Inp 1225.00 NIST
Inp 1223.00 NIST
Inp Outlier 1220.00 NIST
Inp 1225.00 NIST
Inp 1225.00 NIST
Inp 1226.00 NIST
Tboil 466.24 K Relay (1.0) Calculated Property
Tc 651.33 K Relay (1.0) Calculated Property
Tfus 278.06 K Relay (1.0) Calculated Property

Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [249.67; 552.53] 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 A4.12520e+01
Coefficient B8.56080e-01
Coefficient C-3.37400e-04
Coefficient D-7.40000e-09
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 249.67 J/mol×K 273.00 Calculated Property
Cp,gas 301.56 J/mol×K 353.78 Calculated Property
Cp,gas 348.94 J/mol×K 434.56 Calculated Property
Cp,gas 391.80 J/mol×K 515.33 Calculated Property
Cp,gas 430.11 J/mol×K 596.11 Calculated Property
Cp,gas 463.84 J/mol×K 676.89 Calculated Property
Cp,gas 492.97 J/mol×K 757.67 Calculated Property
Cp,gas 517.48 J/mol×K 838.44 Calculated Property
Cp,gas 537.34 J/mol×K 919.22 Calculated Property
Cp,gas 552.53 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0107870; 0.0001885] Pa×s [257.12; 507.99] Joback Predicted correlation Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.27245e+01
Coefficient B2.10712e+03
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentLiquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.257.12
Temperature range, max.507.99
η 0.0107870 Pa×s 257.12 Calculated Property
η 0.0048395 Pa×s 284.99 Calculated Property
η 0.0025045 Pa×s 312.87 Calculated Property
η 0.0014436 Pa×s 340.74 Calculated Property
η 0.0009044 Pa×s 368.62 Calculated Property
η 0.0006051 Pa×s 396.49 Calculated Property
η 0.0004268 Pa×s 424.36 Calculated Property
η 0.0003143 Pa×s 452.24 Calculated Property
η 0.0002398 Pa×s 480.11 Calculated Property
η 0.0001885 Pa×s 507.99 Calculated Property

Similar Compounds

Butanedioic acid, ethyl-(1-methylethyl) ester. Isopropyl butyrate. Propanoic acid, 1-methylethyl ester. Di-tert-butyl butanedioate. Pentanoic acid, 4-oxo-, 1-methylethyl ester. Butanedioic acid, diethyl ester. Glutaric acid, diisopropyl ester. Butanedioic acid, ethyl methyl ester. ethyl propyl succinate. Pentanoic acid, 1-methylethyl ester. Butanedioic acid, dipropyl ester. Isopropyl 3-bromopropanoate. Glutaric acid, ethyl isopropyl ester. Diisopropyl adipate. Ethyl hydrogen succinate.

Find more compounds similar to DIISOPROPYL SUCCINATE.

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.
These property values are available through the Cheméo API. A free account gives you an access key.