Yu Wen
Chen
and
Malcolm Robert
Mackley
*
Department of Chemical Engineering, University of Cambridge, New Museums Site, Pembroke Street, Cambridge, CB2 3RA, UK. E-mail: mrm5@cam.ac.uk
First published on 10th February 2006
Chocolate is a complex soft solid that undergoes a series of physical transformations in the mouth during consumption. Normally chocolate products are manufactured by liquid processing techniques that include ‘melting and casting’ liquid chocolate into moulds as well as enrobing sweet centres with a chocolate outer shell. There is however another method of shape forming chocolate and this review discusses the key elements of a so called ‘cold extrusion’ process. This process involves a combination of pressure and flow, which results in a product with a temporary flexibility. The review covers the basic aspects of the composition and microstructure of chocolate together with experimental observations on the cold extrusion process and the subsequent post extrusion flexibility of the extrudate. Finally some physical insight into the unusual behaviour of chocolate during and after cold extrusion is presented.
Yu Wen Chen | Yu Wen Chen is currently completing a PhD within the Department of Chemical Engineering at Cambridge University on aspects relating to the shape forming of cold extruded chocolate. She obtained her MEng degree in Chemical Engineering at Imperial College London. |
Malcolm Mackley | Malcolm Mackley is a Professor of Process Innovation and heads a Polymer Fluids Group within the Dept. of Chemical Engineering at Cambridge University. His research interests include the rheological aspects of polymer melt extrusion processing, the development of plastic MicroCapillary Film (MCF) and continuous OFM (Oscillatory Flow Mixing) biodiesel and mesoreactors. Prof. Mackley is also currently the President of the British Society of Rheology. |
The idea behind the extrusion of chocolate dates back to the early 1920's when the semi-solid processing of chocolate was first carried out by Laskey, who showed that chocolate could be extruded at high pressures through a die.7 No further work on the semi-solid extrusion of chocolate had been reported until 1994, when Mackley et al.8 described the isothermal extrusion of chocolate below its peak melting temperature and the resulting product possessed a certain short-term flexibility. This temporary flexibility and shape retainment ability of the extrudate immediately after extrusion offer interesting opportunities to form shapes that cannot be manufactured by traditional chocolate production methods. It also raised scientific questions as to why the material behaved in this unexpected and unusual way.
This review briefly describes the basic microstructure of chocolate and the behaviour of chocolate during and after cold extrusion. In addition, the possible link between the mechanical properties of the material and its microstructure is given.
Fig. 1 (a). Schematic representation of the microstructure of chocolate. (b) An optical microscope image of a typical milk chocolate recipe. |
Cocoa butter is composed mainly of triacylglycerols (TAGs) or triglycerides, which are found in most natural oils and fats. TAGs are esters of three fatty acid molecules joined to a glycerol molecule backbone (Fig. 2). The physical and chemical properties of oils and fats are determined by the composition and crystal packing arrangements of the triglycerides. Palmitic (P), stearic (S) and oleic (O) fatty acids, which make up more than 95% (Table 1) of the fatty acids found in cocoa butter,11 combine to form the three main triglycerides POP, SOS and POS (Fig. 2b).
Fig. 2 (a) Basic structure of a triglyceride molecule with a glycerol backbone connected to three fatty acids. (b) Structure of triglyceride POS with the three main fatty acids. |
Fatty acid | Chemical formula | Cocoa butter (%) by wt |
---|---|---|
Palmitic acid (P) | CH3(CH2)14COOH | 26.0 |
Oleic acid (O) | CH3(CH2)7CHCH(CH2)7COOH | 34.8 |
Stearic acid (S) | CH3(CH2)16COOH | 34.4 |
It has been proposed that a certain degree of molecular ordering still exists among the triglygeride molecules of the most stable form just above the melting point of the cocoa butter, usually above 40 °C.12 The chains adopt a chair-like structure which is distorted.13 However the actual structural arrangement of the triglycerides is not yet fully understood and is still a subject of much debate. Figs. 3a and b show, highly schematically, the arrangement of triglyceride molecules in both the solid and the liquid states.
Fig. 3 (a). Schematic structure of cocoa butter in the solid crystalline state (b) A more ‘disorganised’ molecular structure of liquid cocoa butter. |
Most of the melting of cocoa butter occurs over a relatively wide temperature range of between 15 °C and 40 °C (Fig. 4). At 20 °C, about 16% of the triglyceride fats are in the liquid form, hence the semi-solid state of cocoa butter and chocolate at room temperature. Temperatures above 40 °C will result in cocoa butter being predominantly in the molten state. Previous work has proposed that fat crystals and aggregates form a three dimensional network made of interlinked chains and between these solid crystal regions, pools of liquid regions are entrapped.14
Fig. 4 Liquid fat composition in cocoa butter as a function of temperature (ref. 29). |
Fig. 5a shows the schematic diagram of the cold extrusion process using a ram extruder. Filaments of chocolate are extruded with the use of an orifice die (Fig. 5b). Immediately after extrusion, the fresh filaments possess a temporary flexibility that is sufficiently high for the chocolate filament to be tied into knots or coiled into a spring frame (Fig. 6).
Fig. 5 (a) Schematic representation of a ram extruder used in the cold extrusion process. (b) Freshly extruded flexible chocolate filaments at the die exit. |
Fig. 6 (a–b) Freshly extruded chocolate filaments flexible enough to be tied into knots. (c) A spring coil made from extruded chocolate. |
Fig. 7 shows a pressure against time profile obtained during extrusion. The chocolate first goes through a compaction phase where little or no flow occurs. As the piston moves forward, a sharp increase in pressure is observed until the pressure reaches a maximum yield value where the material starts to extrude. At this point, there is a decrease in pressure to a constant value known as the flow pressure. When the piston is stopped, there is an instantaneous decrease in pressure with a further, slow time dependent, relaxation towards a residual pressure. The existence of a residual pressure shows that part of the flow deformation has a characteristic of plastic flow. It has been found that the extrusion pressure is usually independent of the extrusion flow rate20,21 although at temperatures above 26 °C a dependence of the flow pressure with the flow rate develops.8 The flow behaviour of chocolate can therefore be described by a perfect plastic constitutive model20,23,24 where the shear stress of the material is independent of its shear rate, but dependent on the specific composition of the chocolate and temperature.
Fig. 7 Typical variation of pressure with time during a ram extrusion. Piston movement starts at t = 5 s and stops at t = 27 s. (Extrusion T = 20 °C). |
Fig. 8 shows the effect of the piston speed on the flow pressure. The flow pressures for both milk and dark chocolates are essentially independent of the piston speed and the milk chocolate requires lower extrusion pressures than dark chocolate. Studies have shown that the amount of fat phase has a significant effect on the extrusion pressure,20,25 with lower extrusion pressures being associated with high fat phase. The effect of composition on the extrusion pressure has been linked to the amount of liquid or ‘free’ mobile fat present in the chocolate recipe.20 Under similar temperature conditions, milk chocolate has an overall higher liquid fat content than dark chocolate due to the high amount of milk fat present, therefore making it easier to extrude than dark chocolate.
Fig. 8 Effect of piston speed on extrusion pressure. |
Surprisingly, the cold extrusion process itself was found to be essentially isothermal.8,20,23 This resulted in the hypothesis that the considerable work done during extrusion leads to a partial isothermal melting of some crystalline fat and not an increase in the temperature of the extrudate, as might be originally expected. It was however discovered that a transient rise of up to 3 °C in the temperature of the extrudate could occur 2 to 3 min after extrusion as shown in Fig. 9. The latter effect was related to the recrystallisation of the additional liquid fat that had been formed during extrusion.23
Ram extrusion has been used for most of the experimental studies of the cold extrusion process. However screw extrusion is also possible.20,22 The main advantage of cold extrusion is that it offers the possibility of a continuous process for complex shape formation, which was previously difficult to attain with the conventional liquid processing techniques.
Fig. 10 Beam bending tests carried out with a series of solid discs of increasing diameters from left to right. Variation in the flexibility of extruded chocolate shown by the minimum disc curvature the chocolate can sustain without cracking at different post extrusion times. (a) (i)–(iv) tpost = 12 s, 2 min, 5 min, 10 min. (b) Severe cracking and brittle fracture observed in the chocolate at longer post extrusion time tpost = 3 h. |
Fig. 11 Change in the hardness of extruded chocolate with post extrusion time during 45° cone penetrometry tests. (i)–(iv) tpost = 20 s, 5 min, 1 h, 1 day. |
A postulated mechanism for the mechanical and physical processes underlying the cold extrusion is shown schematically in Fig. 12. Before extrusion, the liquid fat is believed to exist in isolated sub-micron domains surrounded by the non-fat solid particles. Once the material reaches yield point under applied pressure, those previously isolated liquid fat domains deform and bond to form ‘internal slip planes’ to allow plastic flow of the material. Indirect experimental evidence20 has shown that some liquid fat migrates to the wall of the barrel and acts as a ‘lubricating layer’ at the wall, hence reducing the frictional resistance at the wall boundary and easing the flow through the die. The creation and the presence of the liquid fat slip planes are thought to make the material temporarily flexible. The chocolate extrudate soon regains its usual hardness and brittleness as the liquid fat recrystallises and reverts back to essentially its original sub-micron domains or microstructure.
Fig. 12 Proposed mechanism governing the cold extrusion process. |
A simple calculation equating the work done during extrusion with the amount of work required to melt a certain crystalline fraction of cocoa butter fat gives a consistent result with the measured changes in the liquid phase during extrusion.8,30 It is therefore clear that cold extrusion involves a mechanically enhanced transition of the crystalline cocoa butter fat to liquid fat phase and hence an associated change in the mechanical properties of the material. Experimental observations8,20,23 have shown that the mechanical work done does not go into heating and increasing the temperature of the chocolate material as might first be expected. At this stage a quantitative model to couple the mechanical characteristics with the phase structure has not been possible and will probably require the future development of experimental techniques that can identify the changes in nano length scale structure within the cocoa butter.
Strategically the cold extrusion processing of chocolate has a number of benefits in that the process is predominantly isothermal and obeys a near perfect plastic extrusion response. This indicates that the extrusion pressure is independent of the extrusion speed and as a result, there is no energy or pressure penalty in extruding at high speed. In addition the extrudate is shape retaining, which means that high precision profiles can be produced from intricate dies. It is plausible to think of cold extruding other materials with a matrix that is the same or comparable to that of cocoa butter, thereby developing a cost effective and continuous shape forming process for different materials with similar interesting soft solid behaviour as described in this review.
This journal is © The Royal Society of Chemistry 2006 |