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Chemical Reaction Engineering ,[object Object],[object Object],[object Object],[object Object]
 
 
Materials on the Web and CDROM ,[object Object]
 
 
 
 
 
Developing Critical Thinking Skills ,[object Object],[object Object],[object Object],[object Object],[object Object]
Let’s Begin CRE ,[object Object]
[object Object],Chemical Identity
[object Object],[object Object],Chemical Identity
[object Object],Chemical Identity 1.  Decomposition
[object Object],Chemical Identity 1. Decomposition 2.  Combination
[object Object],Chemical Identity 1. Decomposition 2. Combination  3.  Isomerization
[object Object],Reaction Rate
[object Object],[object Object],[object Object],[object Object],[object Object],Reaction Rate
Reaction Rate Consider the isomerization  A  B r A  = the rate of formation of species A per unit volume   -r A  = the rate of a disappearance of species A per unit volume  r B  = the rate of formation of species B per unit volume
Reaction Rate ,[object Object],[object Object],[object Object],[object Object]
Reaction Rate ,[object Object],[object Object],[object Object],[object Object]
Reaction Rate ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Reaction Rate ,[object Object],[object Object],[object Object],[object Object],[object Object]
Reaction Rate ,[object Object],[object Object]
Reaction Rate ,[object Object],[object Object]
Reaction Rate ,[object Object],[object Object],[object Object]
Reaction Rate ,[object Object],[object Object],[object Object],[object Object]
General Mole Balance
General Mole Balance
Batch Reactor Mole Balance
CSTR Mole Balance
Plug Flow Reactor
Plug Flow Reactor Mole Balance PFR: The integral form is: This is the volume necessary to reduce the entering molar flow rate (mol/s) from F A0  to the exit molar flow rate of F A .
Packed Bed Reactor  Mole Balance PBR The integral form to find the catalyst weight is:
Reactor Mole Balance Summary
Fast Forward to the Future ,[object Object],[object Object]
Production of Propylene Glycol in an Adiabatic CSTR
What are the exit conversion X  and exit temperature T? Solution Let the reaction be represented by
 
 
 
 
 
 
 
 
KEEPING UP
Separations  These topics do not build upon one another Filtration Distillation Adsorption
Reaction Engineering These topics build upon one another Mole Balance Rate Laws Stoichiometry
Mole Balance Rate Laws Stoichiometry Isothermal Design Heat Effects
Mole Balance Rate Laws
Mole Balance Rate Laws Stoichiometry Isothermal Design Heat Effects
 
 
 
 
 
 
 
 
Batch Reactor Mole Balance
Batch Reactor Mole Balance
Batch Reactor Mole Balance
Batch Reactor Mole Balance
Batch Reactor Mole Balance
Continuously Stirred Tank Reactor  Mole Balance
Continuously Stirred Tank Reactor  Mole Balance
Continuously Stirred Tank Reactor  Mole Balance
C S T R  Mole Balance
CSTR Mole Balance
Plug Flow Reactor
Plug Flow Reactor Mole Balance PFR:
Plug Flow Reactor Mole Balance PFR:
Plug Flow Reactor Mole Balance PFR:
Plug Flow Reactor Mole Balance PFR:
Plug Flow Reactor Mole Balance PFR:
Plug Flow Reactor Mole Balance PFR: The integral form is:
Plug Flow Reactor Mole Balance PFR: The integral form is: This is the volume necessary to reduce the entering molar flow rate (mol/s) from F A0  to the exit molar flow rate of F A .
Packed Bed Reactor Mole Balance PBR
Packed Bed Reactor Mole Balance PBR
Packed Bed Reactor Mole Balance PBR
Packed Bed Reactor Mole Balance PBR
Packed Bed Reactor Mole Balance PBR The integral form to find the catalyst weight is:
Reactor Mole Balance Summary
Reactor Mole Balance Summary
Reactor Mole Balance Summary
Reactor Mole Balance Summary
 
 
 
 
 
 
 
 
 
Chemical Reaction Engineering   Asynchronous Video Series   Chapter 1: General Mole Balance Equation Applied to  Batch Reactors, CSTRs, PFRs, and PBRs H. Scott Fogler, Ph.D.
http://www.engin.umich.edu/~cre
 
 
 
 
 
 
Chemical Reaction Engineering ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Compartments for perfusion Perfusion interactions between compartments are shown by arrows.  V G ,  V L ,  V C , and  V M  are -tissue water volumes for the gastrointestinal, liver, central and muscle compartments, respectively.  V S  is the stomach contents volume.  Stomach V G  = 2.4 l Gastrointestinal V G  = 2.4 l t G  = 2.67 min Liver Alcohol V L  = 2.4 l t L  = 2.4 min Central V C  = 15.3 l t C  = 0.9 min Muscle & Fat V M  = 22.0 l t M  = 27 min
 
Chemical Reaction Engineering ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Reaction Rate Consider the isomerization  A  B r A  = the rate of formation of species A per unit volume
Reaction Rate Consider the isomerization  A  B r A  = the rate of formation of species A per unit volume   -r A  = the rate of a disappearance of species A per unit volume
Reactor Mole Balance Summary

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Chemical reaction engineering