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By R.E. Hayes, J.P. Mmbaga
IntroductionProcess DevelopmentBasic development Blocks of Chemical response EngineeringOutline of the BookIntroduction to Chemical ReactionsClassification and kinds of ReactorsReactor functionality MeasuresIntroduction to fee FunctionTransport Phenomena in ReactorsNumerical MethodsReferencesThe Thermodynamics of Chemical ReactionsBasic DefinitionsEnergy adjustments in SystemsChemical Reaction Read more...
summary: IntroductionProcess DevelopmentBasic development Blocks of Chemical response EngineeringOutline of the BookIntroduction to Chemical ReactionsClassification and kinds of ReactorsReactor functionality MeasuresIntroduction to cost FunctionTransport Phenomena in ReactorsNumerical MethodsReferencesThe Thermodynamics of Chemical ReactionsBasic DefinitionsEnergy alterations in SystemsChemical response EquilibriumSummaryProblemsReferencesMole Balances in excellent ReactorsGeneral Mole stability EquationPerfectly combined Batch ReactorPlug stream ReactorContinuous Stirred Tank ReactorReaction fee by way of Catalyst Mas
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Technical and economic feasibility—Once a new discovery has been made, analysis is usually performed to determine its economic viability. The discovery must offer the promise of a new product, or a new or improved process for manufacturing an existing product. • Commercial reactor development—Once it has been determined that a process offers promise, a reactor must be design. The design will include a determination of the type of reactor to be used and the operating conditions. The design of a reactor requires that the kinetics of the reaction be known, which, in turn, will require the experimental determination of reaction rate parameters.
A wide variety of methods exist for the solutions of such systems. For example, systems of nonlinear equations can be solved using Gauss–Seidel or Newton–Raphson methods, while systems of ODE (initial value problems) can be solved using one of the variants of the Runga–Kutta method. These methods are explained in various books on numerical analysis, for example, Conte and de Boor (1980) and Faires and Burden (1993). It is assumed that the reader is able to use an appropriate numerical method where necessary to solve such systems.
In such a model, the presence of the catalyst is not accounted for in a rigorous way. 6 Reactor Performance Measures When considering the design or operation of a chemical reactor, a quantifiable means of identifying the performance or behavior of a reactor is needed. The performance of a chemical reactor is often related to the extent of reaction that occurs in it, or by the amount of feed that is processed in a given time for a given reactor volume. The first measure gives an indication of the fraction of reactants that are converted into products, while the second gives an indication of the total production rate of the desired product.