Wolfram Demonstrations Project
Housam Binous
« PREVIOUS  |1...13|14|15|16|17|18|19...20|  NEXT »
Demonstrations 301 - 320 of 390
Countercurrent Extraction with Extract Reflux (the Janecke Diagram)Ponchon-Savarit Graphical Method at Total RefluxResidue Curve Map for a Non-Ideal Ternary Mixture with a Distillation BoundaryComputation of the Volume of a CSTR and a PFRPonchon-Savarit Graphical Equilibrium Stage Method
Countercurrent Extraction with Extract Reflux (the Janecke Diagram)
Ponchon-Savarit Graphical Method at Total Reflux
Residue Curve Map for a Non-Ideal Ternary Mixture with a Distillation Boundary
Computation of the Volume of a CSTR and a PFR
Ponchon-Savarit Graphical Equilibrium Stage Method
E-curve and F-curve for the Tanks-in-Series Model of MacMullin and WeberGraphical Method for Evaluating the Performance of N Tanks in SeriesEnthalpy-Concentration Plot for a Benzene-Toluene Binary MixtureVapor Liquid Equilibrium Data for an Ideal Binary MixtureThree-Stage Batch Rectification with Constant Reflux
E-curve and F-curve for the Tanks-in-Series Model of MacMullin and Weber
Graphical Method for Evaluating the Performance of N Tanks in Series
Enthalpy-Concentration Plot for a Benzene-Toluene Binary Mixture
Vapor Liquid Equilibrium Data for an Ideal Binary Mixture
Three-Stage Batch Rectification with Constant Reflux
Cross-Flow Liquid-Liquid ExtractionIsobaric Vapor-Liquid Equilibrium Data of an Immiscible MixtureChemical Reaction and Diffusion in a Spherical Catalyst Pellet (the Nonisothermal Effectiveness Factor)Isobaric Vapor-Liquid Equilibrium Data of a Partially Miscible MixtureSimple Batch Distillation of a Partially Miscible Binary Mixture
Cross-Flow Liquid-Liquid Extraction
Isobaric Vapor-Liquid Equilibrium Data of an Immiscible Mixture
Chemical Reaction and Diffusion in a Spherical Catalyst Pellet (the Nonisothermal Effectiveness Factor)
Isobaric Vapor-Liquid Equilibrium Data of a Partially Miscible Mixture
Simple Batch Distillation of a Partially Miscible Binary Mixture
Batch Rectification of a Partially Miscible Binary MixtureApplication of the Murphree Liquid Efficiency Method to the Study of a Binary Distillation ColumnNonsteady-State Heat Conduction in a CylinderLiquid-Liquid Equilibrium Diagram for a Chloroform-Water-Acetic-Acid Mixture at 25°C and 1 atmAttainable Regions for Maleic Anhydride Manufacture in a Plug-Flow Reactor
Batch Rectification of a Partially Miscible Binary Mixture
Application of the Murphree Liquid Efficiency Method to the Study of a Binary Distillation Column
Nonsteady-State Heat Conduction in a Cylinder
Liquid-Liquid Equilibrium Diagram for a Chloroform-Water-Acetic-Acid Mixture at 25°C and 1 atm
Attainable Regions for Maleic Anhydride Manufacture in a Plug-Flow Reactor

« PREVIOUS  |1...13|14|15|16|17|18|19...20|  NEXT »
 
RELATED RESOURCES
Mathematica »
The #1 tool for creating Demonstrations
and anything technical. 		Wolfram|Alpha »
Explore anything with the first
computational knowledge engine.		MathWorld »
The web's most extensive
mathematics resource.		Course Assistant Apps »
An app for every course—
right in the palm of your hand.
Wolfram Blog »
Read our views on math,
science, and technology.		Computable Document Format »
The format that makes Demonstrations
(and any information) easy to share and interact with.		STEM Initiative »
Programs & resources for
educators, schools & students.		Computerbasedmath.org »
Join the initiative for modernizing
math education.
Powered by Wolfram Mathematica © 2013 Wolfram Demonstrations Project & Contributors  |  Terms of Use  |  Privacy Policy  |  RSSGive us your feedback
Note: To run this Demonstration you need Mathematica 7+ or the free Mathematica Player 7EX
Download or upgrade to Mathematica Player 7EX
I already have Mathematica Player or Mathematica 7+