Chemical Properties of (S)-(+)-1,2-Propanediol (CAS 4254-15-3)

(S)-(+)-1,2-Propanediol

InChI
InChI=1S/C3H8O2/c1-3(5)2-4/h3-5H,2H2,1H3/t3-/m0/s1
InChI Key
DNIAPMSPPWPWGF-VKHMYHEASA-N
Formula
C3H8O2
SMILES
C[C@H](O)CO
Molecular Weight1
76.09
CAS
4254-15-3
Other Names
  • (+)-(S)-1,2-propanediol
  • (+)-1,2-propanediol
  • (S)-1,2-propanediol
  • (S)-Propylene glycol
  • 1,2-(S)-propanediol
  • 1,2-Propanediol, (S)-
  • 1,2-propanediol, (S)-(+)-
  • 3-deoxy-sn-glycerol
  • L(+)-propanediol
  • L-(+)-1,2-propanediol
  • L-(+)-propylene glycol
  • L-1,2-propanediol
  • S(+)-propane-1,2-diol
  • S-(+)-Propylene glycol
  • d-propylene glycol
  • propylene glycol, (S)-(+)-
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Physical Properties

Property Value Unit Source
ω 0.6516 Relay (1.0) Calculated Property
ΔfG° -301.70 kJ/mol Joback Calculated Property
ΔfH°gas -453.50 kJ/mol Relay (1.0) Calculated Property
ΔfusH° 8.18 kJ/mol Joback Calculated Property
ΔvapH° 69.20 ± 0.30 kJ/mol NIST
IE 10.45 eV Relay (1.0) Calculated Property
log10WS 0.47 Relay (1.0) Calculated Property
logPoct/wat -0.640 Crippen Calculated Property
McVol 64.870 ml/mol McGowan Calculated Property
Pc 5791.74 kPa Joback Calculated Property
Tboil 461.55 K Relay (1.0) Calculated Property
Tc 625.27 K Relay (1.0) Calculated Property
Tfus 262.68 K Relay (1.0) Calculated Property
Vc 0.239 m3/kmol Relay (1.0) Calculated Property

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
ΔfusH 8.40 kJ/mol 240.00 NIST
Pvap [4.27e-03; 0.37] kPa [283.50; 338.40] Show Hide
Pvap 4.27e-03 kPa 283.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 6.85e-03 kPa 288.20 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.01 kPa 293.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 9.68e-03 kPa 293.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.01 kPa 297.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.02 kPa 298.20 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.02 kPa 298.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.03 kPa 301.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.02 kPa 301.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.02 kPa 303.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.03 kPa 303.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.03 kPa 305.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.04 kPa 306.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.04 kPa 306.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.05 kPa 309.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.05 kPa 310.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.04 kPa 310.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.04 kPa 310.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.06 kPa 312.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.06 kPa 312.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.07 kPa 313.20 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.07 kPa 313.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.05 kPa 313.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.07 kPa 315.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.09 kPa 316.20 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.09 kPa 316.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.09 kPa 316.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.10 kPa 318.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.09 kPa 318.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.11 kPa 319.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.12 kPa 320.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.10 kPa 320.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.10 kPa 320.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.13 kPa 321.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.14 kPa 322.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.14 kPa 322.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.13 kPa 323.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.16 kPa 323.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.13 kPa 323.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.13 kPa 324.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.17 kPa 325.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.14 kPa 325.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.17 kPa 325.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.18 kPa 326.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.15 kPa 326.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.17 kPa 327.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.20 kPa 327.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.22 kPa 328.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.18 kPa 328.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.18 kPa 328.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.22 kPa 328.60 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.24 kPa 329.50 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.28 kPa 331.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.23 kPa 331.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.26 kPa 333.30 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.30 kPa 335.40 1,2-Propanediol. Comprehensive experimental and theoretical study
Pvap 0.37 kPa 338.40 1,2-Propanediol. Comprehensive experimental and theoretical study

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboilr 460.20 K 102.00 NIST

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [93.81; 211.98] 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 A9.06100e+00
Coefficient B3.62720e-01
Coefficient C-2.03400e-04
Coefficient D4.36000e-08
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 93.81 J/mol×K 273.00 Calculated Property
Cp,gas 113.86 J/mol×K 353.78 Calculated Property
Cp,gas 131.85 J/mol×K 434.56 Calculated Property
Cp,gas 147.93 J/mol×K 515.33 Calculated Property
Cp,gas 162.24 J/mol×K 596.11 Calculated Property
Cp,gas 174.91 J/mol×K 676.89 Calculated Property
Cp,gas 186.08 J/mol×K 757.67 Calculated Property
Cp,gas 195.89 J/mol×K 838.44 Calculated Property
Cp,gas 204.48 J/mol×K 919.22 Calculated Property
Cp,gas 211.98 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.9647802; 0.0002598] Pa×s [230.21; 430.25] 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-1.77150e+01
Coefficient B4.06992e+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.230.21
Temperature range, max.430.25
η 0.9647802 Pa×s 230.21 Calculated Property
η 0.2034137 Pa×s 252.44 Calculated Property
η 0.0551760 Pa×s 274.66 Calculated Property
η 0.0181955 Pa×s 296.89 Calculated Property
η 0.0070031 Pa×s 319.12 Calculated Property
η 0.0030523 Pa×s 341.35 Calculated Property
η 0.0014725 Pa×s 363.57 Calculated Property
η 0.0007726 Pa×s 385.80 Calculated Property
η 0.0004349 Pa×s 408.03 Calculated Property
η 0.0002598 Pa×s 430.25 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.66] kPa [355.11; 484.64] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.64056e+01
Coefficient B-4.61036e+03
Coefficient C-6.90720e+01
Temperature range, min.355.11
Temperature range, max.484.64
Pvap 1.33 kPa 355.11 Calculated Property
Pvap 2.89 kPa 369.50 Calculated Property
Pvap 5.82 kPa 383.89 Calculated Property
Pvap 11.04 kPa 398.29 Calculated Property
Pvap 19.85 kPa 412.68 Calculated Property
Pvap 34.04 kPa 427.07 Calculated Property
Pvap 55.99 kPa 441.46 Calculated Property
Pvap 88.76 kPa 455.86 Calculated Property
Pvap 136.12 kPa 470.25 Calculated Property
Pvap 202.66 kPa 484.64 Calculated Property

Similar Compounds

Propylene Glycol. R-(-)-1,2-propanediol. Glycerin. 3-BROMO-1,2-PROPANEDIOL. 3-Iodo-1,2-propanediol. Propanal, 2,3-dihydroxy-, (S)-. D-(+)-glyceraldehyde. 2,3-Butanediol. DL-2,3-Butanediol. 2,3-Butanediol, [S-(R*,R*)]-. meso-2,3-butanediol. 2,3-Butanediol, [R-(R*,R*)]-. 1,2-Propanediol, 3-chloro-. 1-Propanol, 2-methoxy-. 2-Propanol, 1-methoxy-.

Find more compounds similar to (S)-(+)-1,2-Propanediol.

Sources

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