Скачать презентацию Chemical Reaction Engineering Asynchronous Video Series Chapter 4 Скачать презентацию Chemical Reaction Engineering Asynchronous Video Series Chapter 4

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Chemical Reaction Engineering Asynchronous Video Series Chapter 4, Part 3: Pressure Drop in a Chemical Reaction Engineering Asynchronous Video Series Chapter 4, Part 3: Pressure Drop in a Packed Bed Reactor H. Scott Fogler, Ph. D.

Algorithm for Isothermal Reactor Design 1. Mole Balance and Design Equation 2. Rate Law Algorithm for Isothermal Reactor Design 1. Mole Balance and Design Equation 2. Rate Law 3. Stoichiometry 4. Combine 5. Evaluate

Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a PBR:

Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a PBR: Mole Balance: Must use the differential form of the mole balance to separate variables:

Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a PBR: Mole Balance: Must use the differential form of the mole balance to separate variables: Rate Law: Second order in A and irreversible:

Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a PBR: Mole Balance: Must use the differential form of the mole balance to separate variables: Rate Law: Second order in A and irreversible: Stoichiometry: with T=T 0

Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a Algorithm Analyze the following second order gas phase reaction that occurs isothermally in a PBR: Mole Balance: Must use the differential form of the mole balance to separate variables: Rate Law: Second order in A and irreversible: Stoichiometry: with T=T 0 Combine: Need to find (P/P 0) as a function of W (or V if you have a PFR).

Pressure Drop in Packed Bed Reactors Pressure Drop in Packed Bed Reactors

Pressure Drop in Packed Bed Reactors Ergun Equation: Pressure Drop in Packed Bed Reactors Ergun Equation:

Pressure Drop in Packed Bed Reactors Ergun Equation: Pressure Drop in Packed Bed Reactors Ergun Equation:

Pressure Drop in Packed Bed Reactors Ergun Equation: Pressure Drop in Packed Bed Reactors Ergun Equation:

Pressure Drop in Packed Bed Reactors Ergun Equation: Let Pressure Drop in Packed Bed Reactors Ergun Equation: Let

Pressure Drop in Packed Bed Reactors Ergun Equation: Let Catalyst Weight: Let and Pressure Drop in Packed Bed Reactors Ergun Equation: Let Catalyst Weight: Let and

Multiple Reactions and Pressure Drop Multiple Reactions and Pressure Drop

Multiple Reactions and Pressure Drop In terms of conversion: Multiple Reactions and Pressure Drop In terms of conversion:

Multiple Reactions and Pressure Drop In terms of conversion: Multiple Reactions and Pressure Drop In terms of conversion:

Multiple Reactions and Pressure Drop In terms of conversion: Multiple Reactions and Pressure Drop In terms of conversion:

Analytical Solution Analytical Solution

Analytical Solution Analytical Solution

Analytical Solution Separate Integrate Analytical Solution Separate Integrate

Analytical Solution Separate Integrate For gas phase reactions, as the pressure drop increases, the Analytical Solution Separate Integrate For gas phase reactions, as the pressure drop increases, the concentation decreases, resulting in a decreased rate of reaction, hence a lower conversion when compared to a reactor without a pressure drop.

What if… Dpand Ac change? } } Laminar Turbulent What if… Dpand Ac change? } } Laminar Turbulent

What if… Dpand Ac change? } } Laminar Turbulent What if… Dpand Ac change? } } Laminar Turbulent

What if… Dpand Ac change? } } Laminar Turbulent What if… Dpand Ac change? } } Laminar Turbulent

What if… Dpand Ac change? } } Laminar Turbulent What if… Dpand Ac change? } } Laminar Turbulent

Polymath Solution Polymath Solution

Polymath Solution Polymath Solution

Polymath Solution Polymath Solution

Polymath Solution Polymath Solution