Lydersen method explained

The Lydersen method is a group contribution method for the estimation of critical properties temperature (Tc), pressure (Pc) and volume (Vc). The method is named after Aksel Lydersen who published it in 1955.[1] The Lydersen method is the prototype for and ancestor of many new models like Joback,[2] Klincewicz,[3] Ambrose,[4] Gani-Constantinou[5] and others.

The Lydersen method is based in case of the critical temperature on the Guldberg rule which establishes a relation between the normal boiling point and the critical temperature.

Equations

Critical temperature

T
c=Tb
0.567+\sumGi-\left(\sum
2
G
i\right)

Guldberg has found that a rough estimate of the normal boiling point Tb, when expressed in kelvins (i.e., as an absolute temperature), is approximately two-thirds of the critical temperature Tc. Lydersen uses this basic idea but calculates more accurate values.

Critical pressure

P
c=M
\left(0.34+\sum
2
G
i\right)

Critical volume

Vc=40+\sumGi

M is the molar mass and Gi are the group contributions (different for all three properties) for functional groups of a molecule.

Group contributions

GroupGi (Tc)Gi (Pc)Gi (Vc)GroupGi (Tc)Gi (Pc)Gi (Vc)
bgcolor="#f0f0f0" -CH3,-CH2- 0.020 0.227 55.0>CH 0.012 0.210 51.0
bgcolor="#f0f0f0" -C< - 0,210 41.0 =CH2,#CH 0.018 0,198 45.0
=C<,=C= - 0.198 36.0=C-H,#C- 0.005 0.153 36.0
bgcolor="#f0f0f0" -CH2-(Ring) 0.013 0.184 44.5>CH-(Ring) 0.012 0.192 46.0
>C<(Ring) -0.007 0.154 31.0=CH-,=C<,=C=(Ring)0.011 0.154 37.0
bgcolor="#f0f0f0" -F 0.018 0.22418.0bgcolor="#f0f0f0" -Cl 0.0170.320 49.0
bgcolor="#f0f0f0" -Br 0.0100.50070.0bgcolor="#f0f0f0" -I 0.012 0.83095.0
bgcolor="#f0f0f0" -OH 0.0820.06018.0bgcolor="#f0f0f0" -OH(Aromat)0.031-0.0203.0
bgcolor="#f0f0f0" -O- 0.0210.16020.0bgcolor="#f0f0f0" -O-(Ring) 0.0140.1208.0
>C=O 0.0400.29060.0>C=O(Ring) 0.0330.20050.0
HC=O- 0.0480.33073.0bgcolor="#f0f0f0" -COOH 0.0850.40080.0
bgcolor="#f0f0f0" -COO- 0.0470.47080.0bgcolor="#f0f0f0" -NH2 0.0310.09528.0
>NH 0.0310.13537.0>NH(Ring) 0.0240.09027.0
>N 0.014 0.17042.0>N-(Ring) 0.0070.13032.0
bgcolor="#f0f0f0" -CN 0.0600.36080.0bgcolor="#f0f0f0" -NO2 0.0550.42078.0
bgcolor="#f0f0f0" -SH,-S- 0.0150.27055.0bgcolor="#f0f0f0" -S-(Ring) 0.0080.24045.0
=S 0.0030.24047.0>Si< 0.0300.540-
bgcolor="#f0f0f0" -B< 0.030--

Example calculation

Acetone is fragmented in two different groups, one carbonyl group and two methyl groups. For the critical volume the following calculation results:

Vc = 40 + 60.0 + 2 * 55.0 = 210 cm3

In the literature (such as in the Dortmund Data Bank) the values 215.90 cm3,[6] 230.5 cm3 [7] and 209.0 cm3 [8] are published.

References

  1. Lydersen . a.L. . Estimation of Critical Properties of Organic Compounds . Engineering Experiment Station Report . Madison, Wisconsin . University of Wisconsin College Engineering . 3.
  2. Joback . K.G. . Reid . R.C. . Estimation of pure-component properties from group-contributions . Chemical Engineering Communications . Informa UK Limited . 57 . 1–6 . 1987 . 0098-6445 . 10.1080/00986448708960487 . 233–243.
  3. Klincewicz . K. M. . Reid . R. C. . Estimation of critical properties with group contribution methods . AIChE Journal . Wiley . 30 . 1 . 1984 . 0001-1541 . 10.1002/aic.690300119 . 137–142. 1984AIChE..30..137K .
  4. Book: Ambrose, D.. Correlation and Estimation of Vapour-Liquid Critical Properties. I. Critical Temperatures of Organic Compounds. National Physical Laboratory Reports Chemistry . 92. 1-35. 1978.
  5. Constantinou . Leonidas . Gani . Rafiqul . New group contribution method for estimating properties of pure compounds . AIChE Journal . Wiley . 40 . 10 . 1994 . 0001-1541 . 10.1002/aic.690401011 . 1697–1710. 1994AIChE..40.1697C .
  6. Campbell . A. N. . Chatterjee . R. M. . The critical constants and orthobaric densities of acetone, chloroform, benzene, and carbon tetrachloride . Canadian Journal of Chemistry . Canadian Science Publishing . 47 . 20 . 1969-10-15 . 0008-4042 . 10.1139/v69-646 . 3893–3898. free .
  7. Herz . W.. Neukirch . E.. Zur Kenntnis kritischer Grössen . Zeitschrift für Physikalische Chemie. 104. S.433-450. 1923. 10.1515/zpch-1923-10429 . 99833350 .
  8. Kobe . Kenneth A. . Crawford . Horace R. . Stephenson . Robert W. . Industrial Design Data—Critical Properties and Vapor Presesures of Some Ketones . Industrial & Engineering Chemistry . American Chemical Society (ACS) . 47 . 9 . 1955 . 0019-7866 . 10.1021/ie50549a025 . 1767–1772.