Mass Transfer - Video Lectures
Topic outline
-
-
Announcements Forum
-
-
Relative Volatility and Equilibrium Ratio Page
-
Composition of Ternary System from Relative Volatility Data Page
-
Identifying the State of Mixture - Vapor / Liquid Page
-
Batch Distillation - Composition of Residue Page
-
Batch Distillation - Mole Fraction of Distillate Page
-
Batch Distillation - Moles of Residue Page
-
Batch Distillation - Product Composition vs Time Page
-
Flash Distillation - Feed Composition Page
-
Flash Distillation - Composition and Energy Required Page
-
Partial Condenser Page
-
Maximum Difference between y* and x Page
-
Slope of q-Line Page
-
Reflux Ratio from Vapor Compositions in Successive Trays Page
-
McCabe-Thiele Method - Reflux Ratio and Feed Quality Page
-
Feed Conditions from Operating Lines Data Page
-
Reflux Ratio from Enriching Section Data Page
-
Reflux Ratio and Composition from Material and Energy Data Page
-
Stripping Line of Column with Open Steam Page
-
Composition of Vapor from Column at Total Reflux Page
-
Minimum Number of Trays for a Separation Page
-
Reflux Ratio vs Product Composition Page
-
Number of Trays and Reboiler Heat Load at Minimum Reflux Page
-
Cost vs Reflux Ratio Page
-
Vapor Composition for the given Murphree Efficiency Page
-
Murphree Vapor Efficiency Page
-
Scale-up of Distillation Column Page
-
Distillation of Azeotropic System with Two Columns in Series Page