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BATCHD - Dimensionless Kinetics in a Batch Reactor

An nth-order homogeneous liquid phase reaction is carried out in a batch tank reactor. [Pg.283]

The model is written in both dimensional and dimensionless forms. This example provides experience in the use of dimensionless equations. [Pg.284]

The batch balance for the reactant A with nth-order kinetics is [Pg.284]

Defined in this way, there is no governing dimensionless parameter. [Pg.284]

For a first-order reaction n=l, and the dimensionless time is given by k t. Make a series of runs with different initial concentrations and compare the results, plotting the variables in both dimensional and dimensionless terms. [Pg.285]

5 Simulation Tools and Examples of Chemical Engineering Processes [Pg.288]

For n=2 the dimensionless time is [k t Caq]- Make the runs and study the results as in Exercise 1. Verify that a change in k and a change in Cao have the same influence as long as the product term k Cao is maintained constant. [Pg.289]


BATCHD - Dimensionless Kinetics in a Batch Reactor System... [Pg.235]


See other pages where BATCHD - Dimensionless Kinetics in a Batch Reactor is mentioned: [Pg.283]    [Pg.630]    [Pg.287]    [Pg.283]    [Pg.630]    [Pg.287]   


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