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Multi-response modeling of acrylamide formation in biscuits

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Multi-response modeling of acrylamide

formation in biscuits

E. Capuano1*, H.J. van der Fels-Klerx1, B. Atac-Mogol2, T. Kocadağlı2, N. Göncüoğlu2, B.A. Hamzalıoğlu2, V. Gokmen2

Background

During baking of biscuits potentially harmful compounds might form such as acrylamide (ACR). Kinetic modelling of ACR is a valuable tool for obtaining insight into the mechanism of its formation.

Multi-response modelling, i.e. a modelling approach based on the

fundamental chemical reaction pathways, has the advantage of improving the precision of kinetic parameters estimates while providing insight on the actual reaction mechanism.

Objective

The aim of this study was to model acrylamide formation during baking of biscuits, using multi-response kinetic modelling.

Materials and methods

A biscuit formulation (table 1) was baked in a conventional oven at 200˚C for different times. Concentrations of ACR as well as of

sucrose, glucose, fructose, total free amino acids (AA), and

asparagine were measured in the samples along with moisture

content and temperature. Multi-response modelling was performed using the Athena Visual Studio software package (Athena Visual

Software Inc., Naperville, IL, USA).

Figure 2. Fit of the predicted values to the experimental data for: a)sucrose, b)glucose,

c)fructose, d)total amino acids, e)acrylamide.

Conclusions

A simplified multi-response kinetic model for ACR formation in biscuits baked is proposed which accurately predicts ACR evolution during

baking at 200 °C in the range 12-15 minutes. For its application to the entire time range, additional physical and chemical information beside the chemical reaction network must be incorporated in the model.

Acknowledgements

This research was carried out in the framework of project PROMETHEUS (FP7-KBBE-2010-4).

1 RIKILT Wageningen UR

P.O. Box 230, 6700 AE Wageningen, The Netherlands Contact: edoardo.capuano@wur.nl

T + 31 (0)317 48 02 56

www.wageningenur.nl/en/rikilt

Results

Several kinetic schemes were formulated and applied to the entire

baking time range (0-15 minutes). During baking, sucrose hydrolysis and reducing sugars formation were limited up to 11 minutes after

which a constant increase in sucrose hydrolysis rate occurs. This behaviour could not be accounted for solely by a kinetic reaction

scheme. Only 4 time points (12-15 minutes) were thus considered for further modelling. The changes in moisture content and temperature (<5°C) were negligible in the selected time range. The model that

produced the best fit to the experimental data was selected by a model discrimination analysis based on the posterior probability criterion (figure 1 and 2). In table 2 the optimal estimates for the kinetic parameters is reported.

Ingredient Amount (g)

Wheat flour (standard T55/W150 flour ) 80

Refined palm oil 20

Sucrose 35

NaCl 1

Water 17.6

Sodium bicarbonate 0.8

Ammonium bicarbonate 0.4

Figure 1. Simplified kinetic scheme selected by model discrimination analysis. MRPs=Maillard

reaction products. 0,00 50,00 100,00 12 13 14 15 mmol 100g -1 minutes 0,00 1,00 2,00 3,00 4,00 12 14 mmol 100g -1 minutes 0,00 2,00 4,00 6,00 12 13 14 15 mmol 100g -1 minutes 0 0,05 0,1 0,15 12 13 14 15 mmol 100g -1 minutes 0 0,1 0,2 0,3 0,4 12 13 14 15 μmol 100g -1 minutes

Only fructose contributes to ACR formation. The fraction of asparagine to total AA (Rasp) was approximately constant during baking and the

fraction of asparagine converted to ACR (Facr) is included in the model as a parameter. AA are only degraded upon reaction with fructose

whereas the contribution of intermediate carbonyls from Maillard

reaction is negligible. The fit was good for reducing sugars, total AA and ACR whereas the extent of sucrose hydrolysis was partially

underestimated.

Parameter units Optimal estimate (x102) 95% confidence interval (x102) k1 mmol-1 100g s-1 1.45 ±0.23 k2 s-1 12.4 ±8.90 k3 s-1 8.86 ±7.58 k4 s-1 27 ±5.3 Facr 0.74 ±0.094

Table 1. Composition of the biscuit recipe.

Table 2. Parameters estimate for the selected kinetic model.

2 Hacettepe Un iversity

Department of Food Engineering Hacettepe University

06800 Beytepe, Ankara, Turkey

a

b

c

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