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KINETICS OF DEGRADATION REACTIONS

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Other reaction species are not limiting ... Sorption isotherm: moisture content vs aw. can determine monolayer value (m1) ... There are other sorption isotherm models ... – PowerPoint PPT presentation

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Title: KINETICS OF DEGRADATION REACTIONS


1
KINETICS OF DEGRADATION REACTIONS
2
Kinetics
  • rate of reaction
  • relation between concentration and time

3
Kinetics of a chemical reaction
  • kf
  • aA bB cC dD
  • kb
  • 6 unknowns, need to simplify

4
  • Ass
  • B gtgt A
  • B not limiting
  • kb ltlt kf

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  • Apply in practice not theoretically true.
  • Assumptions
  • Backward reaction is negligible
  • Other reaction species are not limiting
  • Reaction conditions are constant pH, T, aw,
    redox potential, concentration of other species
  • Therefore, k is a pseudo rate constant particular
    for a given food system.

7
Reaction order
  • n 0 A Ao kt
  • B Bo kt
  • n 1 ln A/Ao - kt
  • A Ao e-kt B Bo
    ekt

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10
Units are different, cannot compare.
11
  • Accurate data ? accurate k ? need to measure over
    50 change in reactant species.
  • but in foods 20-30 change is enough for quality
    degradation, can use simple zero order kinetics
  • minimize error in measurements
  • s std. dev.
  • mean value.

12
Half-life time for decrease in quality by
50 If n 1
13
Order determination
  • Method of differentiation

ln dA dt
slopen
lnA
14
  • 2. Method of integration
  • Assume order n 0 or 1 or 2
  • Integrate rate equation, plot equation
  • Evaluate the fit of linear line

15
A
t
16
lnA
t
17
1/A
t
18
  • 3. When n ? 1

19
Microbial growth
First order reaction N number of
microorganisms kG growth rate constant
20
G time for one doubling DG time for 1 log cycle
increase in number of microorganisms G is
determined from the log phase of growth
21
  • Reaction order for some common reactions in foods
  • n 0 enzymatic degradation, lipid oxidation, NEB
  • n 1 microbial growth, rancidity
  • n 2 vitamin C loss
  • For shelf life study
  • Need to determine
  • Quality criteria to be measured
  • Environmental conditions affect the reaction
    rates
  • T, RH

22
Temperature effect
  • Activation energy
  • Arrhenius relation
  • ko Arrhenius equation constant
  • EaActivation energy (cal/mol) excess energy
    barrier to over come
  • R universal gas constant (1.9872 cal/mol K)
  • T absolute temperature, K

23
  • Important points
  • Mode of deterioration changes with temperature
  • Need to have more than two temperatures to obtain
    reliable results
  •  
  • Activation energies for some degradation
    reactions (kcal/mol)
  • Hydrolysis 10-20
  • Lipid oxidation 15-25
  • NEB 20-40
  • Enzymatic or microbial degradation 50-150

24
Temperature effect
  • Q10 value
  • measure of sensitivity to temperature
  • change in rate by 10C change in temperature

25
  • Q10
  • 1.5-2 sensory quality loss in canned foods
  • 1.5-3 rancidity
  • 4-10 browning
  • 20-40 quality loss for frozen fruits and
    vegetables

26
  • Deviations from Arrhenius relation
  •  
  • change in moisture
  • change in physical state, phase change, ice or
    glass formation
  • change in mode of deterioration with T
    increase
  • partitioning of reactants between two phases,
    such as concentration of reactants upon
    freezing
  • temperature history effects

27
Temperature effect
  • Tg considerations
  • T lt Tg glassy, Arrhenius model
  • Tg - (Tg 100C) rubbery, WLF model
  • T gt Tg 100C solution, Arrhenius model
  • slope of Arrhenius plot changes,
    William-Landel-Ferry (WLF) equation applies which
    empirically models T dependence of mechanical and
    dielectric relaxations within the rubbery state.

28
ln k
Arrhenius
rubbery Ea 45.1 kcal/mol
glassy Ea 20.8 kcal/mol
Tg
1/T
NEB Model System (Nelson and Labuza, 1994) Break
in the Arrhenius plot due to changes in the
properties of the rubbery and glassy systems
29
  • In diffusioncontrolled systems
  • where diffusion is free volume dependent, WLF
    equation is needed to express reaction rate
    constants as a function of T.

30
Calculate kg from known Tg and the average
coefficients C1 and C2. To find real C1 and C2
use 2nd equation
kref rate constant at Tref gt Tg C1, C2
system-dependent coefficients. C1 -17.44 C2
51.6 for Tref Tg for various polymers
31
  • 10-100?C above Tg
  • diffusion-dependent changes in food quality
  • viscosity, crystallization, textural changes fit
    WLF model.
  • In model systems,
  • deterioration reactions seen to occur at T lt Tg
  • oxidation, NEB, ascorbic acid degradation
  • therefore, porosity of the system, physical
    changes such as collapse and crystallization
    should be considered

32
  • But chemical reactions may be kinetically and/or
    diffusion limited. How to decide which equation
    to use?
  • Effective reaction rate constant k
    k/(1k/?D)
  • D Diffusion coefficient
  • ? constant, independent of T
  • k Arrhenius-type T dependence constant
  • D follows Arrhenius equation with a change in
    slope at Tg, or follow WLF equation in the
    rubbery state and especially in the range
    10-100?C above Tg,
  • k/?D defines relative influence of k and D.
  • If k/?D lt 0.1 Arrhenius equation can be used for
    modeling T dependency.
  • Slope changes in Arrhenius plot at Tg with either
    constant slope above Tg or with a gradually
    changing slope.
  • For complex food systems involving multiple
    reaction steps and phases, either model can be
    used for controlled-temperature functions like
    sine, square wave T fluctuations to verify the
    shelf life model.

33
Temperature effects
  • Fluctuating temperatures
  • sine wave
  • square wave

34
aw and temperature
  • Clasius-Clapeyron equation describes temperature
    dependence of aw

35
BET equation
  • Brunauer-Emmett-Teller equation
  • Sorption isotherm moisture content vs aw
  • can determine monolayer value (m1)
  • valid for aw 0 - 0.5

36
GAB equation
  • valid for aw 0 - 0.9
  • can determine monolayer value
  • There are other sorption isotherm models
  • Need to find which fits for particular food using
    experimental data

37
Moisture gain or loss
  • Can estimate changes in moisture in packaged
    foods
  • k/x permeability of the package

38
Kinetics of enzymatic reactions
  • k1 k2
  • E S ES E P
  • k-1

P
Vo
t
39
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40
Michaelis Menten equation
41
Kinetics of enzymatic reactions
  • Vmax Maximum velocity when enzyme is saturated
    with substrate
  • Km Substrate concentration at half maximum
    velocity, (k-1 k2) / k1

Vmax/2
42
  • Use linear form of the equation to find Km and
    Vmax
  • 6-10 substrate concentration
  • So 0.1Km-10Km
  • Lineweaver-Burk method

1/Vo
?Km/Vmax
1/Vmax
-1/Km
1/So
43
Linear regression
  • To estimate changes in a quality index with time
  • Need to fit experimental data to equations and
    calculate equation parameters
  • Can convert equations to linear form
  • Use statistics for fitting data to equations
  • accurate estimates of the parameters

44
Linear regression
  • Relation of a dependent variable y with an
    independent variable x
  • y bo b1x
  • bo , b1 parameters to estimate
  • y a quality index
  • x time
  • Assumptions
  • 1. Data are normally distributed
  • 2. Constant variance
  • 3. Independence of error
  • 4. Linear relation

45
Linear regression
Minimize sum of squares of error
46
Linear regression
  • More data more accurate prediction
  • df degree of freedom, depend on number of data,
    more data more df
  • lose 1 df to estimate 1 parameter
  • confidence level (1-?) 90, 95, 99

47
Linear regression
  • t?/2 a test statistic, student t value at a
    given confidence level
  • If n 3 df 1 t?/2 at 95 12.71
  • If min n 8 df 6 t?/2 2.45

48
Linear regression
  • Confidence interval for a parameter estimate
  • change in the parameter estimate

49
Linear regression
  • Correlation Coefficient (R2)
  • Proportion of variability in y explained by the
    linear relation
  • Total variability in y
  • variability explained by linear relation
    residuals
  • R2 lt 1

50
Linear regression
  • Strength of a linear relation
  • 1. Small confidence intervals for parameter
    estimates
  • 2. High Correlation Coefficient (R2) 1
  • If R2 is small
  • 1. no relation between x and y
  • 2. relation not linear, use nonlinear equations
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