Title: Chemical Reaction Engineering
1Chemical Reaction Engineering
2Kinetics 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.
3Reaction 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
4Reaction 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
5Rate 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.
6Reaction 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)
7Rate 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)
8General Mole Balance
9Batch Reactor Mole Balance
10Constantly Stirred Tank Reactor Mole BalanceCSTR
or MFR
11Plug 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.
12Packed Bed Reactor Mole Balance
PBR
The integral form to find the catalyst weight is
13Space 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
14Reactor Mole Balance Summary
15Reactor Mole Balance Summary
16Reactor Mole Balance Summary
17Reactor Mole Balance Summary
18Reactor Mole Balance Summary
19Conversion
- 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
20Batch Reactor Conversion
21CSTR Conversion
Algebraic Form
There is no differential or integral form for a
CSTR.
22PFR Conversion
PFR
Differential Form
Integral Form
23Design Equations
24Reactor 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
25Reactor Sizing (PFR)
For PFR th evolume of the reactor needed is
given by the area under the curve
area
26Summary
27Rate 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)
28Examples of Rate Laws
- First Order Reactions
- (1) Homogeneous irreversible elementary gas
phase reaction - with
-
-
29Examples of Rate Laws
- First Order Reactions
- (1) Homogeneous irreversible elementary gas
phase reaction - with
-
- (2) Homogeneous reversible elementary
reaction -
-
-
- with
and
30Examples 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
31Examples of Rate Laws
- Second Order Reactions
- (2) Homogeneous irreversible elementary
reaction
with
32Examples 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