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Inès BIRLOUEZ-ARAGON
Optimization of a roasting processOptimization of a roasting process
by means of rapid monitoring of quality by means of rapid monitoring of quality
indicators and kinetic modellingindicators and kinetic modelling
Food Factory 2010 - Sweden
Processing contaminants in food : a new challenge for the Food Industry
• Processing contaminants: A recent history Severe heat treatments concerned
• No regulation at the moment: But recommendations from the EC for surveying levels
• Monitoring in final food products: Expensive analytical methods Delay in obtaining results
• Process optimization: Mitigate contaminants while maintaining the sensorial properties of the product
Food Factory 2010 - Sweden
Situation 8 years after discoveryof acrylamide in food products
Food Factory 2010 - Sweden
Potato crisps, instant coffee, and substitute coffee products, such as Potato crisps, instant coffee, and substitute coffee products, such as those based on barley or chicory, all showed significantly higher levels those based on barley or chicory, all showed significantly higher levels of acrylamide in 2008 compared to 2007.of acrylamide in 2008 compared to 2007.
EFSA survey of acrylamide in food products indicates that voluntary EFSA survey of acrylamide in food products indicates that voluntary efforts to reduce levels of the carcinogen are working but only in a limited efforts to reduce levels of the carcinogen are working but only in a limited number of food groups:number of food groups:
Roasted Chicory : p to 2000 µg/kg Roasted Chicory : p to 2000 µg/kg
the product with highest acrylamide levelsthe product with highest acrylamide levels
Chicory root Chicory root Roasted ChicoryRoasted Chicory
Reactional system
Food Factory 2010 - Sweden
SaccharoseSaccharose →→HeatHeat
5%5% + H2O+ H2O
InulineInuline →→ Fructose ↔ GlucoseFructose ↔ Glucose65% 65%
Fructose + GlucoseFructose + Glucose
HeatHeat + H2O+ H2O
HMFHMF MelanoïdinesMelanoïdines(without nitrogen)(without nitrogen)
CaramelisationCaramelisation
HMFHMF
+ AA+ AA MelanoïdinesMelanoïdines
(with nitrogen)(with nitrogen)
MaillardMaillard
Amino acidAmino acid
- 3 H2O- 3 H2O
MaillardMaillard
MaillardMaillard
To mitigateTo mitigate
Needed for sensorial propertiesNeeded for sensorial properties
AsparagineAsparagine
AcrylamideAcrylamide
The drying process initiates reactions.
Food Factory 2010 - Sweden
0
2
4
6
8
10
12
14
16
18
20
Ra_Fr_d09 Se_Fr_d09 Ra_Fr_m09 Se_Fr_m09 Ra_Fr_f09 Se_Fr_f09 Ra_Be_09 Se_Be_09
g / 10
0g M
S
Fructose Glucose Saccharose
0
20
40
60
80
100
120
140
160
180
Ra_Fr_d09 Se_Fr_d09 Ra_Fr_m09 Se_Fr_m09 Ra_Fr_f09 Se_Fr_f09 Ra_Be_09 Se_Be_09
g / 10
0g M
S
Asparagine
==
FF
DD
FF
FFFF
DD
DD
DD
FF
DD
FF
FF
FF
DDDD
DD
Sugar degradation : Sugar degradation : formation of carbonyl substrates ? formation of carbonyl substrates ?
Asparagine formationAsparagine formation
0
20
40
60
80
100
120
140
160
180
0 15 30 45 60 75 90 105 120 135 150 165 170 176 182
Tem
péra
ture
(°C)
Temps (min)
Série A Série M Série N
The roasting process
Food Factory 2010 - Sweden
3 burners3 burners
2 burners2 burners
1 burner1 burner
Target colourTarget colour
Dry chicory was roasted by Dry chicory was roasted by Chicorée du Nord Chicorée du Nord according to a standard process .according to a standard process .
Roasting process originates browningvia HMF and melanoïdins formation
Food Factory 2010 - Sweden
0,0
0,5
1,0
1,5
2,0
2,5
3,0
3,5
0
2
4
6
8
10
12
0 50 100 150 200
HMF
(mg/
g)
mg/
100g
de M
S
Température (min)
Glucose + Fructose
Saccharose
HMF
Bell shape of acrylamide formation:importance of the cooling process
Food Factory 2010 - Sweden
(( µg/
kgµ
g/kg
) )
AcrylamideAcrylamide
AsparagineAsparagine
Cooling Cooling processprocess
Complete destructionComplete destructionof asparagine of asparagine
Process Modelling and optimisation regarding acrylamide
1- Development of a fluorescence predictionmodel to monitor acrylamide under various roasting conditions
Food Factory 2010 - Sweden
Prediction model : acrylamide (µg/kg)Prediction model : acrylamide (µg/kg)8% error8% error
Predicted valuesPredicted values
Mea
sure
d va
lues
(LC
-MS
)M
easu
red
valu
es (
LC-M
S)
FLUORALYSFLUORALYSThe food quality parameters in one FLASH The food quality parameters in one FLASH
9 different roasting processes and 3 reproductions
Food Factory 2010 - Sweden
0
500
1000
1500
2000
2500
A : 127 kW
3>2>1>0 brûleurs
B : 117 kW
T°amb
D : 117 kW 40°C
E : 3>2 brûleurs
F : 3 brûleurs
G : 147 kW
H : 127 kW
I : 127 kW
3>2>1>0 brûleurs
L: 127 kW 3>1>0
brûleurs
M : reproA,
N : reproA,
ACR
(
µg/kg)
ACR PREDIT
Acrylamide between 1000 and 2200 µg/kg depending on the roasting conditionsAcrylamide between 1000 and 2200 µg/kg depending on the roasting conditionsInitial T°; heat energy; time on different heat energiesInitial T°; heat energy; time on different heat energieserror of reproducibility : 25% including raw materialerror of reproducibility : 25% including raw material
Reaction modelling:prediction of acrylamide using apparent reaction kinetics
Asparagine Asparagine Acrylamide Acrylamide degradation productsdegradation productsk1k11st order1st order
Food Factory 2010 - Sweden
Process modelling:prediction of browning using apparent reaction kineticsprediction of browning using apparent reaction kinetics
substratessubstrates browning browning k1k10 order0 order
Food Factory 2010 - Sweden
Simulation of the processInitial T° : 60°C
Two steps T° increase : change at 70min
Food Factory 2010 - Sweden
augmentation de température avant le changement de consigne (°C/min)
augm
enta
tion
de t
empé
ratu
re a
près
le c
hang
emen
t de
con
sign
e (°
C/m
in)
quantité d'acrylamyde prédite (µg/g) en fonction du procédé
0 0.2 0.4 0.6 0.8 10
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
500
1000
1500
2000
2500
3000
3500
4000
augmentation de température avant le changement de consigne (°C/min)
augm
enta
tion d
e t
em
péra
ture
aprè
s le c
hangem
ent
de c
onsig
ne (
°C/m
in)
couleur (U.A.) en fonction du procédé
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
1000
2000
3000
4000
5000
6000
7000
8000
Acrylamide formationAcrylamide formation BrowningBrowning
T°
incr
eas
e in
the
sec
ond
heat
ing
step
T°
incr
eas
e in
the
sec
ond
heat
ing
step
T°
incr
eas
e in
the
sec
ond
heat
ing
step
T°
incr
eas
e in
the
sec
ond
heat
ing
step
T° increase in the first heating stepT° increase in the first heating step T° increase in the first heating stepT° increase in the first heating step
Cooling once the target colour has been reachedCooling once the target colour has been reachedT° always lower than 160°CT° always lower than 160°C
Optimization of the process
zone optimale (A<100)+(M>200)+((C>8500)&(C<9000))+(Tmax<160))
augmentation de température avant le changement de consigne (°C/min)
augm
enta
tion d
e t
em
péra
ture
aprè
s le c
hangem
ent
de c
onsig
ne (
°C/m
in)
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 10
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
1
1.5
2
2.5
3
3.5
4
OptimalOptimalzone zone
Food Factory 2010 - Sweden
Conclusion
• Rapid acrylamide monitoring provides a rich data base for reaction
modelling (280 analyses with only 50 conventional acrylamide assessments).
• Simple reaction modelling makes it possible to simulate
colour and acrylamide formation during chicory roasting.
• Optimisation of the process provides the time-T° zone whereminimal acrylamide is formed while colour is maintained.
• Further experimental assays based on the Fluoralys sensor
will make it possible to reach acryalmide levels below 1000 µg/kg
while maintaining product sensorial properties. Food Factory 2010 - Sweden
Rapid Methods 2010 - The Netherlands
Chicorée du Nord for the roasting experiments and samples;Chicorée du Nord for the roasting experiments and samples;
CSIC (Fran Morales) for conventional analysis of acrylamide and CSIC (Fran Morales) for conventional analysis of acrylamide and
AgroParisTech (Bertrand Heyd) for process simulation and optimisation.AgroParisTech (Bertrand Heyd) for process simulation and optimisation.
Thanks to …