Fig. 2.1

Developing the mathematical model of the reaction in Mathcad

Fig. 2.2.

Using the reduced stoichiometric matrix

Fig. 2.3.

Developing the mathematical model using the Maple suits

Maple 9

Fig. 2.4.

Developing the reduced mathematical model

Fig. 2.5.

Solving the direct kinetic problem by the matrix method: forming the necessary matrices

Fig. 2.6.

Calculating the vector of the substance current concentrations

Fig. 2.7.

The Laplace transformation in Mathcad

Fig. 2.8.

Applying the operator method to derivation of the kinetic curve equation for the intermediate of the consecutive reaction

Fig. 2.9.

The operator method in Maple

Maple 9

Fig. 2.10.

Solving the system of the linear differential equations by means of the operator method

Fig. 2.11.

Kinetics of the two-step first-order consecutive reaction with the reversible second step

Fig. 2.12.

The time dependence of the reactant concentration in the stirred tank reactor

Fig. 2.13.

The cascade of the stirred tank reactors

Fig. 2.14.

Modeling the transient regime in the system of three reactors

Fig. 2.15.

Replacing the source function with the linear combination of the functions

Fig. 2.16.

Solving the direct problem for the reaction complicated by the photochemical conversion

Fig. 2.17.

Checking applicability of the steady-state concentration method

Fig. 2.18.

The analysis of the monomolecular reaction mechanism

Fig. 2.19.

The symbolic evaluation of the intermediate steady-state concentrations

Fig. 2.20.

Deriving the right part of the reduced differential equation system for ethane cracking

Fig. 2.21.

Derivation of the equation for the source reactant kinetic curve

Maple9

Fig. 2.22.

The kinetic curves of the stable participants of the ethane cracking process

Fig. 2.23.

Checking the quasi-equilibrium principle

Fig. 2.24.

Derivation of the kinetic equations for the enzyme reaction