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Collection and Analysis of Rate Data
Dr. AKM Shafiqul Islam
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Types of Chemical Reactions
Two types of reaction for rate data The Batch reactor, which is used primarily for homogenous reaction The Differential reactor, which is used for solid-fluid heterogeneous reactions
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Batch Reaction In Batch reaction experiments, concentration, pressure, and or volume are usually measured and recorded at the different times during the course of reaction. Measurements on the differential reactor are made during steady-state operation. The product concentrations are monitored for different sets of feed conditions
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Rate law A B 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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Example, A B If B is being created at a rate of 0.2 moles per decimeter cubed per second, i.e., the rate of formation of B is, rB = 0.2 mole/dm3/s Then A is disappearing at the same rate: -rA = 0.2 mole/dm3/s the rate of formation of A is rA = -0.2 mole/dm3/s
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Power Law Model & Elementary Rate Laws
The dependence of reaction rate, -rA on the concentration of the species present fn(Cj) The order of a reaction refers to the powers to which the concentrations are raised in the kinetic rate law Here a order with respect to reactant A and b order with respect to reactant B
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Steps in Analyzing Rate Data
Postulate a rate law Power law models for homogenous reactions Langmuir-Hinshelwood models or heterogeneous reactions
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Select reactor type and corresponding mole balance
If batch reactor use mole balance on Reactant A TE5-1.1 If different PBR use mole balance on product P (AP) TE5-1.2
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Process your data in terms of measured variable (e.g., NA, CA or PA)
If possible write your mole balance in terms of the measured variable Look for simplifications For example, if one of the reactant is excess, assume its concentration is constant. If the gas phase mole fraction of reactant is small, set e0
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For a batch reactor, calculate –rA as function of concentration CA to determine reaction order
Differential analysis Combine the mole balance and power law model (TE5-1.3) (TE5-1.4)
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taking the natural log (TE5-1.5) Find from CA versus t data by
Graphical method Finite differential method Polynominal Plot vs dt and find reaction order a which Find k
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For the combined mole balance and rate law is
Integral method For the combined mole balance and rate law is (TE5-1.4) Guess a and integrate equation Nonlinear regression (Polymath) Integrate equation (TES5-1.4) to obtain (TE5-1.6)
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For differential PBR calculate as a function of and
Calculate as a function of reactant concentration Choose model, e.g., Use nonlinear regression to find the best model and model parameters Analyze the rate model for “goodness of fit”.
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Batch Reactor Data Batch reactors are used primarily to determine rate law parameters for homogeneous reactions Determination is achieved by measuring concentration as a function of time Use differential, integral and nonlinear regression method of data analysis to determine reaction order, a and specific reaction rate constant, k
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if reaction is irreversible, it is possible to determine reaction order a and the specific rate constant by either nonlinear regression or numerically differentiating concentration vs time data Example, for the decomposition reaction A Products The differential method may be used
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It is possible to determine the relationship between and the concentration of other reactants
For irreversible reaction A + B Products with the rate law Where a and b are both unknown, the reaction could first be run in an excess of B so that CB remains essentially unchanged during the course of the reaction
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Where After determining a, the reaction is carried out in excess of A, for which the rate law is approximated as
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Once a and b are determined, kA can be calculated from the measurement of –rA at known concetration of A and B Both a and b can be determined by using method of excess, coupled with a differential analysis of data for batch system
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Differential Method of Analysis
Consider a reaction carried out isothermally in a constant-volume batch reactor and concentration recorded as a function of time. By combining the mole After taking natural log on both side of the equation
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The reaction order can be found from a ln-ln plot of
vs
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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
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Graphical Method The graphical method involves plotting –DCA/Dn as a function of t and then using equal-area differentiation to obtain –dCA/dt.
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concentration (mol/dm3)
Numerical differentiation Numerical differentiation formulas can be used when the data points in the independent variables are equally spread, such as t1 – t0 = t2 – t1 = Dt time (s) t1 t2 t3 concentration (mol/dm3) CAo CA1 CA2 CA3
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The three-point differentiation formulas
Initial point: Interior points: Last point:
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Polynomial Fit Another technique to differentiate the data is to first fit the concentration-time data to the nth-order polynomial: CA = ao + a1t + a2t2 + a3t3 +a4t4 Many software package program that will calculate best values for the constants ai only by entering concentration-time data
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After determining the constants, ai, the differentiate equation with respect to time can get
The concentration and the time rate of change of concentration are both known at any time t
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