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SEMI-SOLIDPROCESSING OF CHOCOLATE
AND COCOA BUTTER
:
Rheology and Microstructure
Anas Ejaz Shaikh
13FET1006
Department of Food Engineering &
Technology
Institute of ChemicalTechnology
Introduction
Chocolate
Products
Moulded Chocolate Products
[Viscous with yield stress and
mild shear thinning
characteristics]
Cooling Demoulding
Packaging
30ā°C
Chocolate
Products
Cold Extruded Chocolate
Products
Convergent die
5 to 25 ā° C
Isothermal
[No detectable
temperature change]
Example of the development of barrel pressure during a ram extrusion of
chocolate, measured in the MultiPass Rheometer just upstream of extrusion
die.
Solid line: barrel pressure. Broken line: piston position.
Microstructure
of Chocolate
Cocoa butter /
milk fat
Sucrose Cocoa
particles
Milk
particles
Surface
active
ingredients
[e.g.,
lecithin]
Flavours
[e.g.,
vanillin]
Crystals :
Assumed to
remain
unchanged
Semi-
crystalline fat
matrix ofTGs
Plastic Flow
and Mouthfeel
of Chocolate
Fraction of
crystal phase
triglycerides
liquid state
work dissipation
(cold extrusion)
Flow &
flexible
response
Work by Beckett et al., 1994
Work by Mulji et al.,2003
NMR techniques
Liquid fraction of cocoa
butter decreased
Indicating that:
it had increased during extrusion
Literature Survey
Inference from Literature
Survey
Increase in liquid
phase content
Recovery to the
original crystal
fraction
Post-extrusion
During-extrusion
This forms the basis of the present study
Objectives of Current Study
ā€¢ To subject chocolate or cocoa butter to successive multiple
extrusions using a double-piston Multi Pass Rheometer
ā€¢ To establish how the material responds to different process
histories
ā€¢ To probe the crystal fraction of the fat matrix present at any
time using X-ray diffraction technique from which the liquid
fraction can be obtained
Scope of the Study
ā€¢The coupled data (MPR + XRD) gives
insight into the way processing
influences both :
1) The rheology of the materials.
2) The microstructure of the materials.
Materials and Experimental
Techniques
ā€¢ Materials :
1) Chocolate
2) Cocoa Butter
ā€¢ Multi-Pass Rheometer
ā€¢ Extrusion Loading & Operation Protocol
Chocolate
Solid Granules (x < 5mm) of Milk Chocolate
[Nestle ProductTechnology CentreYork (York, UK)]
Cocoa butter
Multi-Pass Rheometer
ļ±Repeated processing of samples at a
con-trolled temperature and mean
hydrostatic pressure that can be fixed
by moving the pistons towards each
other
ļ±Two pressure transducers enable
time-dependent measurements of
differential pressure between them
ļ±In addition to these process
rheology measurements, it is possible
to use the MPR3 together with an X-
ray scattering facility
ļ±Beryllium capillary (to allow
sufficient transmission of X-rays)
ļ±Simultaneous measurements of
microstructure and process rheology
Extrusion Loading
Chocolate and Cocoa butter were in granular/powder form at the
temperature of interest
Aim :To maintain the particular polymorphic form of
the crystalline triglyceride molecules
Melting the chocolate
and solidifying it in the
instrument
Requires a well-
controlled ā€˜temperingā€™
Granules compacted in a medical
syringe made of plastic (from which the
front part had been sawn off)
Fed from this syringe into the bottom
and top sections of the MPR and into
the wide parts of the capillary section
Operation Protocol
1) Compaction Phase
2) Extrusion sequences
The temperature of the barrel system was kept constant at
20 +/- 1ā°C
Results and Discussion
Experimental Observations of 4 Interrelated effects
Mechanical
Softening
Re-
hardening
Melting of
TGs
Re-
crystallisation
ofTGs
Studied through Rheological
changes by differential
pressure measurements
Multi pass
Extrusion
Single pass
Extrusion
Studied through
Structural changes
by in situ XRD
experiments
Extrusion Softening
High Stress (Viscous fluid but softer
than the reference)
Low Stresses
(Rigid)
1) The initial extrusion shows the highest extrusion pressure and
subsequent extrusion strokes show a progressive decay.
2) After approximately 20 extrusions, no substantial further change of
the extrusion pressure profile occurred.
ļ±The behaviour of cocoa butter is very similar to that of chocolate
ļ±A progressive decay in extrusion pressure with increasing number of passes
and a final plateau where the extrusion pressure is essentially independent
on the amount of further processing cycles
ļ±Softening is a consequence of changes in triglyceride matrix of chocolate
Re-hardening
Principle:
Generally, work softening of a material can be fully or partially reversible (thixotropic
materials) or irreversible, depending on whether the material can return to an
equilibrium state within the time scale of the observation
If the work softening were an irreversible effect then it would be expected that the
delay time would have no influence on the observed extrusion pressure evolution
No change in Pextrusion =
Irreversible work softening
ļ±The data shows for both chocolate and cocoa butter that if the delay time is short, the extrusion pressure does not
recover, however if the delay time is of order 40 min, near complete recovery of the extrusion pressure is reached.
ļ±For the case of chocolate ā€˜re-hardenedā€™ chocolate with delay times tdelay >2 min required an even higher peak
pressure to initiate flow than for unprocessed chocolate, presumably due to the compaction of the chocolate during
extrusion.
Both the multi-pass experiments
with no time delay
with finite time delay
show that the PROCESS BEHAVIOUR of the
semi-solid chocolate and cocoa butter is sensitive
(i) to
the amount of work that has been applied
and
(ii) to
the time between application of this work and further
processing.
Inference
Microstructure Changes: Melting and Re-crystallization
Problem (Effect)
A difficulty in
applying X-ray
diffraction to study
triglyceride
crystallization in
chocolate
Problem (Cause)
Presence of sugar crystals as
their strong diffraction peaks
mask some of the
characteristic diffraction
peaks of the triglyceride
crystals
Solution
Focussing on the
ā€˜long spacingsā€™ of
triglyceride crystals, where
sugar crystals
do not contribute to the
diffraction pattern
Ī²1 -3
ā€˜Form VIā€™
Ī²2 -3
ā€˜Form Vā€™
1) No other long spacings were
observed in our experiments,
indicating that no significant
crystallization other triglyceride
polymorphs occurred.
2) Furthermore, in all our experiments
the changes of these two peaks
were proportional to each other,
indicating that they corresponded
to the same crystal form.
Principle :
If we assume that the diffraction peaks
correspond to a single crystal form,
the integrated intensity, i.e.,
the area under all the peaks,
should be proportional to the crystal content.
Processing-induced Melting :
(i) Not a function of processing flow rate (piston velocity)
(ii) A function of Work dissipated during extrusion due to
extrusion pressure
Recovery in the crystal fraction of the triglycerides after extrusion a series of X-
ray data was obtained at different times after the extrusion had stopped
Recovery time for:
1) Chocolate : 40 min
2) Cocoa butter : 10 min
Conclusions
ā€¢ Systematic extrusion sequences using a multi-pass rheometer
have shown that milk chocolate at ambient temperature is
softened considerably by extrusion processing.
ā€¢ In situ X-ray characterization of the triglyceride matrix in milk
chocolate during and after extrusion showed a processing-
induced melting of triglyceride crystals which re-crystallized
during the ā€˜rest periodā€™ after an extrusion.
Contribution to the Society
ā€¢ A step ahead in the Semi-solid processing of
Chocolate and Cocoa butter
ā€¢ Study of kinetics for formation of extruded
chocolate products with better mouthfeel
ā€¢ The Experimental Correlation of Process
Rheology with Microstructure
Future Scope
ā€¢ Characterization of the cold extrusion of
chocolate using a perfect plastic model with a
constant plastic yield stress is insufficient to
completely describe the processing
behaviour.
ā€¢ An extended model that includes :
1) Effect of work-induced phase changes and
their effect on the rheological properties of
chocolate
2) Prediction of the local solid and liquid phase
contents of the triglycerides
Chocolate Rheology - Anas Shaikh - 13FET1006

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Chocolate Rheology - Anas Shaikh - 13FET1006

  • 1. SEMI-SOLIDPROCESSING OF CHOCOLATE AND COCOA BUTTER : Rheology and Microstructure Anas Ejaz Shaikh 13FET1006 Department of Food Engineering & Technology Institute of ChemicalTechnology
  • 2. Introduction Chocolate Products Moulded Chocolate Products [Viscous with yield stress and mild shear thinning characteristics] Cooling Demoulding Packaging 30ā°C Chocolate Products Cold Extruded Chocolate Products Convergent die 5 to 25 ā° C Isothermal [No detectable temperature change]
  • 3. Example of the development of barrel pressure during a ram extrusion of chocolate, measured in the MultiPass Rheometer just upstream of extrusion die. Solid line: barrel pressure. Broken line: piston position.
  • 4. Microstructure of Chocolate Cocoa butter / milk fat Sucrose Cocoa particles Milk particles Surface active ingredients [e.g., lecithin] Flavours [e.g., vanillin] Crystals : Assumed to remain unchanged Semi- crystalline fat matrix ofTGs Plastic Flow and Mouthfeel of Chocolate
  • 5. Fraction of crystal phase triglycerides liquid state work dissipation (cold extrusion) Flow & flexible response Work by Beckett et al., 1994 Work by Mulji et al.,2003 NMR techniques Liquid fraction of cocoa butter decreased Indicating that: it had increased during extrusion Literature Survey
  • 6. Inference from Literature Survey Increase in liquid phase content Recovery to the original crystal fraction Post-extrusion During-extrusion This forms the basis of the present study
  • 7. Objectives of Current Study ā€¢ To subject chocolate or cocoa butter to successive multiple extrusions using a double-piston Multi Pass Rheometer ā€¢ To establish how the material responds to different process histories ā€¢ To probe the crystal fraction of the fat matrix present at any time using X-ray diffraction technique from which the liquid fraction can be obtained
  • 8. Scope of the Study ā€¢The coupled data (MPR + XRD) gives insight into the way processing influences both : 1) The rheology of the materials. 2) The microstructure of the materials.
  • 9. Materials and Experimental Techniques ā€¢ Materials : 1) Chocolate 2) Cocoa Butter ā€¢ Multi-Pass Rheometer ā€¢ Extrusion Loading & Operation Protocol
  • 10. Chocolate Solid Granules (x < 5mm) of Milk Chocolate [Nestle ProductTechnology CentreYork (York, UK)]
  • 12. Multi-Pass Rheometer ļ±Repeated processing of samples at a con-trolled temperature and mean hydrostatic pressure that can be fixed by moving the pistons towards each other ļ±Two pressure transducers enable time-dependent measurements of differential pressure between them ļ±In addition to these process rheology measurements, it is possible to use the MPR3 together with an X- ray scattering facility ļ±Beryllium capillary (to allow sufficient transmission of X-rays) ļ±Simultaneous measurements of microstructure and process rheology
  • 13. Extrusion Loading Chocolate and Cocoa butter were in granular/powder form at the temperature of interest Aim :To maintain the particular polymorphic form of the crystalline triglyceride molecules Melting the chocolate and solidifying it in the instrument Requires a well- controlled ā€˜temperingā€™ Granules compacted in a medical syringe made of plastic (from which the front part had been sawn off) Fed from this syringe into the bottom and top sections of the MPR and into the wide parts of the capillary section
  • 14. Operation Protocol 1) Compaction Phase 2) Extrusion sequences The temperature of the barrel system was kept constant at 20 +/- 1ā°C
  • 15. Results and Discussion Experimental Observations of 4 Interrelated effects Mechanical Softening Re- hardening Melting of TGs Re- crystallisation ofTGs Studied through Rheological changes by differential pressure measurements Multi pass Extrusion Single pass Extrusion Studied through Structural changes by in situ XRD experiments
  • 16. Extrusion Softening High Stress (Viscous fluid but softer than the reference) Low Stresses (Rigid)
  • 17. 1) The initial extrusion shows the highest extrusion pressure and subsequent extrusion strokes show a progressive decay. 2) After approximately 20 extrusions, no substantial further change of the extrusion pressure profile occurred.
  • 18. ļ±The behaviour of cocoa butter is very similar to that of chocolate ļ±A progressive decay in extrusion pressure with increasing number of passes and a final plateau where the extrusion pressure is essentially independent on the amount of further processing cycles ļ±Softening is a consequence of changes in triglyceride matrix of chocolate
  • 19. Re-hardening Principle: Generally, work softening of a material can be fully or partially reversible (thixotropic materials) or irreversible, depending on whether the material can return to an equilibrium state within the time scale of the observation If the work softening were an irreversible effect then it would be expected that the delay time would have no influence on the observed extrusion pressure evolution No change in Pextrusion = Irreversible work softening
  • 20. ļ±The data shows for both chocolate and cocoa butter that if the delay time is short, the extrusion pressure does not recover, however if the delay time is of order 40 min, near complete recovery of the extrusion pressure is reached. ļ±For the case of chocolate ā€˜re-hardenedā€™ chocolate with delay times tdelay >2 min required an even higher peak pressure to initiate flow than for unprocessed chocolate, presumably due to the compaction of the chocolate during extrusion.
  • 21. Both the multi-pass experiments with no time delay with finite time delay show that the PROCESS BEHAVIOUR of the semi-solid chocolate and cocoa butter is sensitive (i) to the amount of work that has been applied and (ii) to the time between application of this work and further processing. Inference
  • 22. Microstructure Changes: Melting and Re-crystallization Problem (Effect) A difficulty in applying X-ray diffraction to study triglyceride crystallization in chocolate Problem (Cause) Presence of sugar crystals as their strong diffraction peaks mask some of the characteristic diffraction peaks of the triglyceride crystals Solution Focussing on the ā€˜long spacingsā€™ of triglyceride crystals, where sugar crystals do not contribute to the diffraction pattern Ī²1 -3 ā€˜Form VIā€™ Ī²2 -3 ā€˜Form Vā€™ 1) No other long spacings were observed in our experiments, indicating that no significant crystallization other triglyceride polymorphs occurred. 2) Furthermore, in all our experiments the changes of these two peaks were proportional to each other, indicating that they corresponded to the same crystal form.
  • 23. Principle : If we assume that the diffraction peaks correspond to a single crystal form, the integrated intensity, i.e., the area under all the peaks, should be proportional to the crystal content.
  • 24. Processing-induced Melting : (i) Not a function of processing flow rate (piston velocity) (ii) A function of Work dissipated during extrusion due to extrusion pressure
  • 25. Recovery in the crystal fraction of the triglycerides after extrusion a series of X- ray data was obtained at different times after the extrusion had stopped Recovery time for: 1) Chocolate : 40 min 2) Cocoa butter : 10 min
  • 26. Conclusions ā€¢ Systematic extrusion sequences using a multi-pass rheometer have shown that milk chocolate at ambient temperature is softened considerably by extrusion processing. ā€¢ In situ X-ray characterization of the triglyceride matrix in milk chocolate during and after extrusion showed a processing- induced melting of triglyceride crystals which re-crystallized during the ā€˜rest periodā€™ after an extrusion.
  • 27. Contribution to the Society ā€¢ A step ahead in the Semi-solid processing of Chocolate and Cocoa butter ā€¢ Study of kinetics for formation of extruded chocolate products with better mouthfeel ā€¢ The Experimental Correlation of Process Rheology with Microstructure
  • 28. Future Scope ā€¢ Characterization of the cold extrusion of chocolate using a perfect plastic model with a constant plastic yield stress is insufficient to completely describe the processing behaviour. ā€¢ An extended model that includes : 1) Effect of work-induced phase changes and their effect on the rheological properties of chocolate 2) Prediction of the local solid and liquid phase contents of the triglycerides