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Chemical Reaction Engineering

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Title: Chemical Reaction Engineering


1
Chemical Reaction Engineering
  • Dr. Yahia Alhamed

2
Kinetics and Reaction Rate
  • What is reaction rate?
  • It is the rate at which a species looses its
    chemical identity per unit volume.
  • The rate of a reaction can be expressed as-
  • - The rate of disappearance of a reactant or
  • - The rate of appearance of a product.

3
Reaction Rate
Consider species A
-rA the rate of formation of species A per unit
volume
rB the rate of formation of species B per unit
volume
EXAMPLE If B is being formed at 0.2 moles per
decimeter cubed per second, ie, rB 0.2
mole/dm3/s Then A is disappearing at the same
rate -rA 0.2 mole/dm3/s The rate of formation
(generation of A) is rA -0.2 mole/dm3/s
4
Reaction Rate
  • Consider species j
  • rj is the rate of formation of species j per unit
    volume e.g. mol/dm3s
  • rj is a function of concentration, temperature,
    pressure, and the type of catalyst (if any)
  • rj is independent of the type of reaction system
    (batch, plug flow, etc.)
  • rj is an algebraic equation, not a differential
    equation

5
Rate Law Basics
  • A rate law describes the behavior of a reaction.
    The rate of a reaction is a function of
    temperature (through the rate constant) and
    concentration.

6
Reaction Rate for solid catalytic reactions
  • For a catalytic reaction, we refer to -rA', which
    is the rate of disappearance of species A on a
    per mass of catalyst basis.
  • -r'A rA/bulk density of the catalyst (?b)

7
Rate Law Basics
  • A rate law describes the behavior of a reaction.
    The rate of a reaction is a function of
    temperature (through the rate constant) and
    concentration.
  • Power Law Model
  • k is the specific reaction rate (constant)
  • k is given by the Arrhenius Equation
  • WhereE activation energy (cal/mol)
  • R gas constant (cal/molK)
  • T temperature (K)
  • A frequency factor (units of A, and k, depend
    on overall reaction order)

8
General Mole Balance
9
Batch Reactor Mole Balance
10
Constantly Stirred Tank Reactor Mole BalanceCSTR
or MFR
11
Plug Flow Reactor (PFR) Mole Balance
The integral form is
This is the volume necessary to reduce the
entering molar flow rate (mol/s) from FA0 to the
exit molar flow rate of FA.
12
Packed Bed Reactor Mole Balance
PBR
The integral form to find the catalyst weight is
13
Space time and space velocity
  • FA0 CAo vo
  • ? is called space time (s) V/vo
  • Space velocity 1/?, where
  • FA0 Molar feed rate of key reactant A (mol/s)
  • CAo Concentration of key reactant A in the feed
    (mol/m3)
  • voVolumetric flow rate of feed to the reactor
    (m3/s)
  • V volume of the reactor
  • For constant volume systems v vo where v is
    volumetric flow rate leaving the reactor

14
Reactor Mole Balance Summary
15
Reactor Mole Balance Summary
16
Reactor Mole Balance Summary
17
Reactor Mole Balance Summary
18
Reactor Mole Balance Summary
19
Conversion
  • Consider the general reaction aA bB -?cC
    dD
  • We will choose A as bases of calculation (i.e.
    Key reactant)
  • The limiting reactant is usually taken as the key
    reactant
  • Then A (b/a)B ? (c/a)C (d/a)D
  • XA moles reacted/moles fed

20
Batch Reactor Conversion
21
CSTR Conversion
Algebraic Form
There is no differential or integral form for a
CSTR.
22
PFR Conversion
PFR
Differential Form
Integral Form
23
Design Equations
24
Reactor Sizing (CSTR)
  • Given -rA as a function of conversion, -rAf(X),
    one can size any type of reactor.
  • We do this by constructing a Levenspiel plot.
  • Here we plot either as a
    function of X.
  • volume of a CSTR is

25
Reactor Sizing (PFR)
For PFR th evolume of the reactor needed is
given by the area under the curve
area
26
Summary
27
Rate Law Basics
  • A rate law describes the behavior of a reaction.
    The rate of a reaction is a function of
    temperature (through the rate constant) and
    concentration.
  • Power Law Model
  • k is the specific reaction rate (constant)

28
Examples of Rate Laws
  • First Order Reactions
  • (1) Homogeneous irreversible elementary gas
    phase reaction
  • with

29
Examples of Rate Laws
  • First Order Reactions
  • (1) Homogeneous irreversible elementary gas
    phase reaction
  • with
  • (2) Homogeneous reversible elementary
    reaction
  • with
    and

30
Examples of Rate Laws
  • First Order Reactions
  • (1) Homogeneous irreversible elementary gas
    phase reaction
  • with
  • (2) Homogeneous reversible elementary
    reaction
  • with
    and
  • Second Order Reactions
  • (1) Homogeneous irreversible non-elementary
    reaction
  • with and
  • This is first order in ONCB, first order in
    ammonia and overall second order.

At 188C
31
Examples of Rate Laws
  • Second Order Reactions
  • (2) Homogeneous irreversible elementary
    reaction

with
32
Examples of Rate Laws
  • Second Order Reactions
  • (2) Homogeneous irreversible elementary
    reaction
  • This reaction is first order in CNBr, first order
    in CH3NH2 and overall second order.
  • (3) Heterogeneous catalytic reaction The
    following reaction takes place over a solid
    catalyst

with
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