Barlow's law: Difference between revisions

From formulasearchengine
Jump to navigation Jump to search
en>Addbot
m Bot: Migrating 1 interwiki links, now provided by Wikidata on d:q4184771
en>Trappist the monk
Line 1: Line 1:
The '''Lydersen method'''<ref>Lydersen a.L., “Estimation of Critical Properties of Organic Compounds“, University of Wisconsin College Engineering, Eng. Exp. Stn. Rep. 3, Madison, Wisconsin</ref> is a [[group contribution method]] for the estimation of critical properties temperature ([[Critical temperature|T<sub>c</sub>]]), pressure ([[Critical pressure|P<sub>c</sub>]]) and volume (V<sub>c</sub>). The Lydersen method is the prototype for and ancestor of many new models like [[Joback method|Joback]],<ref>Joback K.G., Reid R.C., “Estimation of pure-component properties from group-contributions”, Chem.Eng.Commun., 57, 233-243, 1987
</ref> [[Klincewicz method|Klincewicz]],<ref>Klincewicz K. M., Reid R. C., "Estimation of Critical Properties with Group Contribution Methods", AIChE Journal, 30(1), 137-142, 1984</ref>
Ambrose,<ref>Ambrose D., “Correlation and Estimation of Vapour-Liquid Critical Properties. I. Critical Temperatures of Organic Compounds”, Nat.Phys.Lab.Rep.Chem., Rep.No. 92, 1-35, 1978
</ref>
Gani-Constantinou<ref>Constantinou L., Gani R., “New Group Contribution Method for Estimating Properties of Pure Compounds”, AIChE J., 40(10), 1697-1710, 1994
</ref> 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 ==
He is identified by the name of Vincent Arrieta and he absolutely enjoys this name. New Hampshire is his [http://Www.Wonderhowto.com/search/start+location/ start location]. The matter he adores most is [http://Imgur.com/hot?q=modelling+trains modelling trains] but he's been having on new issues currently. His career is a money officer. Go to his web site to uncover out more: http://www.neuhaus-partner.ch/cuteeditor_files/themes/office2003blue/images/files/office/nike-air-max-90-le.html<br><br>Feel free to visit my blog ... [http://www.neuhaus-partner.ch/cuteeditor_files/themes/office2003blue/images/files/office/nike-air-max-90-le.html Nike Air Max 90 Le]
 
=== Critical temperature ===
<math>T_c=\frac{T_b}{0.567+\sum G_i-\left(\sum G_i\right)^2}</math>
 
Guldberg has found that a rough estimate of the [[normal boiling point]] ''T''<sub>b</sub>, when expressed in [[kelvins]] (i.e., as an [[absolute temperature]]), is approximately two-thirds of the critical temperature ''T''<sub>c</sub>. Lydersen uses this basic idea but calculates more accurate values.
 
=== Critical pressure ===
<math>P_c=\frac{M}{\left(0.34+\sum G_i\right)^2}</math>
 
=== Critical volume ===
<math>V_c\,=\,40+\sum G_i</math>
 
M is the [[molar mass]] and G<sub>i</sub> are the group contributions (different for all three properties) for [[functional group]]s of a [[molecule]].
 
== Group contributions ==
{| cellpadding="4" rules="all" style="margin: 1em 0em; background: #ffffff; border: 2px solid #aaa;"
|- align="center" bgcolor="#f0f0f0"
!Group
!G<sub>i</sub> (T<sub>c</sub>)
!G<sub>i</sub> (P<sub>c</sub>)
!G<sub>i</sub> (V<sub>c</sub>)
!Group
!G<sub>i</sub> (T<sub>c</sub>)
!G<sub>i</sub> (P<sub>c</sub>)
!G<sub>i</sub> (V<sub>c</sub>)
|- align="center"
| bgcolor="#f0f0f0" |-CH3,-CH2- ||0.020 ||0.227 ||55.0
| bgcolor="#f0f0f0" |>CH ||0.012 ||0.210 ||51.0
|- align="center"
| bgcolor="#f0f0f0" |-C< ||- ||0,210 ||41.0
| bgcolor="#f0f0f0" |=CH2,#CH ||0.018 ||0,198 ||45.0
|- align="center"
| bgcolor="#f0f0f0" |=C<,=C= ||- ||0.198 ||36.0
| bgcolor="#f0f0f0" |=C-H,#C- ||0.005 ||0.153 ||36.0
|- align="center"
| bgcolor="#f0f0f0" |-CH2-(Ring) ||0.013 ||0.184 ||44.5
| bgcolor="#f0f0f0" |>CH-(Ring) ||0.012 ||0.192 ||46.0
|- align="center"
| bgcolor="#f0f0f0" |>C<(Ring) ||-0.007 ||0.154 ||31.0
| bgcolor="#f0f0f0" |=CH-,=C<,=C=(Ring)||0.011 ||0.154 ||37.0
|- align="center"
| bgcolor="#f0f0f0" |-F ||0.018 ||0.224||18.0
| bgcolor="#f0f0f0" |-Cl ||0.017||0.320 ||49.0
|- align="center"
| bgcolor="#f0f0f0" |-Br ||0.010||0.500||70.0
| bgcolor="#f0f0f0" |-I ||0.012 ||0.830||95.0
|- align="center"
| bgcolor="#f0f0f0" |-OH ||0.082||0.060||18.0
| bgcolor="#f0f0f0" |-OH(Aromat)||0.031||-0.020||3.0
|- align="center"
| bgcolor="#f0f0f0" |-O- ||0.021||0.160||20.0
| bgcolor="#f0f0f0" |-O-(Ring) ||0.014||0.120||8.0
|- align="center"
| bgcolor="#f0f0f0" |>C=O ||0.040||0.290||60.0
| bgcolor="#f0f0f0" |>C=O(Ring) ||0.033||0.200||50.0
|- align="center"
| bgcolor="#f0f0f0" |HC=O- ||0.048||0.330||73.0
| bgcolor="#f0f0f0" |-COOH ||0.085||0.400||80.0
|- align="center"
| bgcolor="#f0f0f0" |-COO- ||0.047||0.470||80.0
| bgcolor="#f0f0f0" |-NH2 ||0.031||0.095||28.0
|- align="center"
| bgcolor="#f0f0f0" |>NH ||0.031||0.135||37.0
| bgcolor="#f0f0f0" |>NH(Ring) ||0.024||0.090||27.0
|- align="center"
| bgcolor="#f0f0f0" |>N ||0.014 ||0.170||42.0
| bgcolor="#f0f0f0" |>N-(Ring) ||0.007||0.130||32.0
|- align="center"
| bgcolor="#f0f0f0" |-CN ||0.060||0.360||80.0
| bgcolor="#f0f0f0" |-NO2 ||0.055||0.420||78.0
|- align="center"
| bgcolor="#f0f0f0" |-SH,-S- ||0.015||0.270||55.0
| bgcolor="#f0f0f0" |-S-(Ring) ||0.008||0.240||45.0
|- align="center"
| bgcolor="#f0f0f0" |=S ||0.003||0.240||47.0
| bgcolor="#f0f0f0" |>Si< ||0.030||0.540||-
|- align="center"
| bgcolor="#f0f0f0" |-B< ||0.030||-||-
| bgcolor="#f0f0f0" |          ||      ||      ||
|}
 
== Example calculation ==
[[File:AcetonGruppen.PNG|Group assignment for Acetone]]
 
[[Acetone]] is fragmented in two different groups, one carbonyl group and two methyl groups. For the critical volume the following calculation results:
 
V<sub>c</sub> = 40 + 60.0 + 2 * 55.0 = 210&nbsp;cm<sup>3</sup>
 
In the literature<ref>[[Dortmund Data Bank]]</ref> the values 215.90&nbsp;cm<sup>3</sup>,<ref>Campbell A.N., Chatterjee R.M., Can.J.Chem., 47(20), S. 3893-3898, 1969</ref> 230.5&nbsp;cm<sup>3</sup> <ref>Herz W., Neukirch E., Z.Phys.Chem.(Leipzig), 104, S.433-450, 1923</ref> and 209.0&nbsp;cm<sup>3</sup> <ref>Kobe K.A., Crawford H.R., Stephenson R.W., Ind.Eng.Chem., 47(9), S. 1767-1772, 1955</ref> are published.
 
== References ==
<references/>
 
[[Category:Thermodynamic models]]

Revision as of 03:05, 4 March 2014


He is identified by the name of Vincent Arrieta and he absolutely enjoys this name. New Hampshire is his start location. The matter he adores most is modelling trains but he's been having on new issues currently. His career is a money officer. Go to his web site to uncover out more: http://www.neuhaus-partner.ch/cuteeditor_files/themes/office2003blue/images/files/office/nike-air-max-90-le.html

Feel free to visit my blog ... Nike Air Max 90 Le