2- mole balances_stu

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Chemical Reaction Engineering (CRE) is the field that TODAY’S LECTURE Introduction Definitions General Mole Balance Equation

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Page 1: 2- Mole Balances_stu

Chemical Reaction Engineering (CRE) is the field that…

TODAY’S LECTURE

Introduction

Definitions

General Mole Balance Equation

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Chemical Reaction Engineering

Chemical reaction engineering is at the heart of virtually every chemical process. It separates the chemical engineer from other engineers.

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Let’s Begin CRE

Chemical Reaction Engineering (CRE) is the field that …..

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• A chemical species is said to have reacted when it has lost its chemical identity.

Chemical Identity

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• A chemical species is said to have reacted when it has lost its chemical identity.

1. Decomposition

Chemical Identity

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• The reaction rate is the rate at which a species looses its chemical identity per unit volume.

Reaction Rate

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Reaction Rate

Consider the isomerization AB

rA = the rate of formation of species A per unit volume

-rA = the rate of a disappearance of species A per unit volume

rB = the rate of formation of species B per unit volume

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Reaction Rate

• EXAMPLE: AB If Species B is being formed at a rate of

0.2 moles per decimeter cubed per second, ie,

rB = 0.2 mole/dm3/s

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Reaction Rate

• For a catalytic reaction, we refer to -rA',

which is the rate of disappearance of

species A on a per mass of catalyst basis.

(mol/gcat/s)

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Reaction Rate

Consider species j:

• rj is the rate of formation of species j per unit volume [e.g. mol/dm3/s]

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General Mole Balance

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General Mole Balance

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Batch Reactor Mole Balance

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Batch Reactor Mole Balance

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Continuously Stirred Tank Reactor Mole Balance

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CSTR (Cont.)

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Plug Flow Reactor

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PFR Mole Balances

PFR:

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PFR Mole Balances (Cont.)

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PFR Mole Balances (Cont.)

PFR:

The integral form is:

V dFAr

AFA 0

FA

This is the volume necessary to reduce the entering molar flow rate (mol/s) from FA0 to the

exit molar flow rate of FA.

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Packed Bed Reactor Mole Balance

PBR

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PBR Mole Balances (Cont.)

PBR

FA0 FA r AdW dNA

dt

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Reactor Mole Balance Summary

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KEEPING UP

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Separations

These topics do not build upon one another

Filtration Distillation Adsorption

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Reaction Engineering

These topics build upon one another

Mole Balance Rate Laws Stoichiometry

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Mole Balance Rate Laws

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Mole Balance

Rate Laws

Stoichiometry

Isothermal Design

Heat Effects

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Homework 1: A 200-dm3 constant-volume batch reactor is pressurized to 20 atm with a mixture of 75% A and 25% inert. The gas-phase reaction is carried out isothermally at 227 C.

V = 200-dm3

P = 20 atmT = 227 C 

a. Assuming that the ideal gas law is valid, how many moles of A are in the reactor initially? What is the initial concentration of A? b. If the reaction is first order:

Calculate the time necessary to consume 99% of A.c. If the reaction is second order:

Calculate the time to consume 80% of A. Also calculate the pressure in the reactor at this time if the temperature is 127 C.

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Homework 2: