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- Q955351 subject Q7156671.
- Q955351 subject Q8382210.
- Q955351 abstract "The Fenske equation in continuous fractional distillation is an equation used for calculating the minimum number of theoretical plates required for the separation of a binary feed stream by a fractionation column that is being operated at total reflux (i.e., which means that no overhead product distillate is being withdrawn from the column).The equation was derived in 1932 by Merrell Fenske, a professor who served as the head of the chemical engineering department at the Pennsylvania State University from 1959 to 1969.When designing large-scale, continuous industrial distillation towers, it is very useful to first calculate the minimum number of theoretical plates required to obtain the desired overhead product composition.".
- Q955351 thumbnail Total_Reflux.png?width=300.
- Q955351 wikiPageExternalLink distill4.html.
- Q955351 wikiPageExternalLink 74_LiuQuantrilleCheng1993df.pdf.
- Q955351 wikiPageExternalLink 25%20-%20MULTICOMPONENT%20DISTILLATION%20CONCEPTS%20.ppt.
- Q955351 wikiPageWikiLink Q101017.
- Q955351 wikiPageWikiLink Q11345.
- Q955351 wikiPageWikiLink Q125264.
- Q955351 wikiPageWikiLink Q1436074.
- Q955351 wikiPageWikiLink Q1863368.
- Q955351 wikiPageWikiLink Q1949855.
- Q955351 wikiPageWikiLink Q220089.
- Q955351 wikiPageWikiLink Q241687.
- Q955351 wikiPageWikiLink Q2661322.
- Q955351 wikiPageWikiLink Q2712833.
- Q955351 wikiPageWikiLink Q498526.
- Q955351 wikiPageWikiLink Q5109383.
- Q955351 wikiPageWikiLink Q559549.
- Q955351 wikiPageWikiLink Q7156671.
- Q955351 wikiPageWikiLink Q739627.
- Q955351 wikiPageWikiLink Q83588.
- Q955351 wikiPageWikiLink Q8382210.
- Q955351 wikiPageWikiLink Q840492.
- Q955351 wikiPageWikiLink Q866399.
- Q955351 wikiPageWikiLink Q898610.
- Q955351 wikiPageWikiLink Q901363.
- Q955351 wikiPageWikiLink Q908990.
- Q955351 comment "The Fenske equation in continuous fractional distillation is an equation used for calculating the minimum number of theoretical plates required for the separation of a binary feed stream by a fractionation column that is being operated at total reflux (i.e., which means that no overhead product distillate is being withdrawn from the column).The equation was derived in 1932 by Merrell Fenske, a professor who served as the head of the chemical engineering department at the Pennsylvania State University from 1959 to 1969.When designing large-scale, continuous industrial distillation towers, it is very useful to first calculate the minimum number of theoretical plates required to obtain the desired overhead product composition.".
- Q955351 label "Fenske equation".
- Q955351 depiction Total_Reflux.png.