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• Constant-volume of batch reactor1. Differential method of analysis of data
2. Integral method of analysis of data
3. Method of Initial Rates
4. Method of Half-Lives
• Varying-volume batch reactor
TOPIC 2
Determination of Rate Law
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• Constant-volume of batch reactor1. Differential method of analysis of data
- Graphical Differentiation
- Numerical Differentiation
- Polynomial-fit Differentiation
1. Integral method of analysis of data
TOPIC 2 (PART 1)
Determination of Rate Law
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Constant volume of batch reactor refer to volume of
reaction mixture, not the volume of the reactor.
It also known as constant-density reaction system.
The measure of reaction rate of component ibecomes
For ideal gas
therefore,
*This means the rate of
reaction of a
component can be
given by the rate of
change of concentration
or partial pressure
[1]
[2]
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• Say A, converted to something else, or the fraction of Areacted away. We call this, simply, the conversion of A,with symbol X A .
• Suppose that N A0 is the initial amount of A in the reactorat time t = 0, and that N A is the amount present at timet. Then the conversion of A in the constant volumesystem is given by
The Conversion
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• and
• We will develop the equations in this chapter in terms of
concentration of reaction components and also in terms
of conversions.• Later we will relate X A and C A for the more general case
where the volume of the system does not stay constant.
[7]
[8]
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For irreversible reaction, the reaction order α andspecific rate constant can be determined by
.
It is applicable when the rate is essentially a functionof the concentration of only .
Consider a reaction carried out isothermally in a
constant volume batch reactor and the concentration
is as a function of time.
A A kC r
P A
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– Combine mole balance and rate law:
– The reaction order can be found by taking the natural
logarithm of both side
A A
AC k
dt
dC
A A
AC k
dt
dC lnlnln
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• Three Ways to Determine (-dCA/dt) from
Concentration-Time Data: – Graphical differentiation
– Numerical differentiation
– Differentiation of a polynomial fit to the data
FAKULTI OF CHEMICALENGINEERING, UiTM CHE584/594
9
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Graphical Method
• This method accentuates measurement error!
time (s) 0 t1 t2 t3
concentration(mol/dm3)
CAo CA1 CA2 CA3
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Numerical Method• Can be used when the data points in the independent
variable are equally spaced.
• dCA/dt can be calculated by
– Initial point
– Interior points
– Last point
time (s) 0 t1 t2 t3 t4 t5
concentration
(mol/dm3)CAo CA1 CA2 CA3 CA4 CA5
t t t t t 1201
t
C C C
dt
dC A A A
t
A
2
43210
0
112
1
i Ai A
t
AC C
t dt
dC
i
543
5
34
2
1
A A A
AC C C
t dt
dC
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• The integral method of analysis always puts a particularrate equation to the test bythe with the
.
• If the fit is unsatisfactory, another rate equation is. This procedure is shown and used
in the cases next treated.
• It should be noted that the integral method is
especially useful for fitting simple reaction typescorresponding to .
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• Consider the reaction
Irreversible Unimolecular-Type
First-Order Reactions
[9]
• For this reaction. Separating and integrating we obtain
[11]
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• In terms of conversion (see Eqs. 7 and 8), the rate
equation, Eq. 10, becomes
•
which on rearranging and integrating gives
[12]
Or
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• A plot of , as shown in Fig.
below.
• If the experimental data seems to be better fitted by a
curve than by a straight line,
because the first-order reaction
.
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• Integral Method Rate Analysis
•
We could integrate the combined mole balanceand rate law to plot reaction rate data in terms of
concentration vs. time for 0, 1st, and 2nd order
reactions.
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• Zero order
• First order