Formulario de Reactores Heterogéneos Segundo Parcial

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2. Introd Ec Diseño de

1

of 4

Formulario de reactores heterogéneos segundo parcial

           () ()        ()      ()     *   +       

1 Ec. de diseño

2 ley cinética

3 Estequiometria

4 Combinación

Ec. De Ergun forma analítica

Ecuación de Ergun

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                                                         

Orden 2

Relaciones para difusividades

    Knudsen

        

Definición de actividad

Resistencia externa de la transferenc

Reactores multifasicos Velocidad de absorción del gas

Trasporte en el granulo de catalizador

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     √   √    √   √  

Difusión y reacción Modulo de Thiele

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2. Introd Ec Diseño de

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 √    √  

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                     √    Para orden n

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Cinética falsa

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