Parameters Influencing Cocrystallization and Polymorphism in Milk Fat 899
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View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by RERO DOC Digital Library Parameters Influencing Cocrystallization and Polymorphism in Milk Fat Birgit Breitschuh and Erich J. Windhab* Institute of Food Engineering, Department of Food Science, Swiss Federal Institute of Technology (ETH), 8092 Zurich, Switzerland ABSTRACT: Dry fractionation of milk fat is a common tech- spans from about −40 to 40°C. Furthermore, the composition nique used to produce fat fractions with physical properties that changes with season, region, and feeding (4). These physical are suitable for a variety of food and pharmaceutical products. properties and variations restrict the use of milk fat in food During milk fat fractionation, the partial crystallization of tria- and pharmaceutical or cosmetic products. To overcome these cylglycerols from the melt is the most important step. The effi- limitations, fractionation is performed (5). The techniques ciency of the separation of the crystals from the suspension is used for fractionation are varied. They are reviewed by also important, but the crystallization itself influences the chem- Kreulen (6), Deffense (7), and Hamm (8). The most common ical composition and thereby determines the properties of the crystal fraction. At low supercooling, the crystallization kinetics dry fractionation is the separation of triacylglycerols on the are slow, and thus process time is increased. With increased ki- basis of their melting ranges. A single-step fractionation netics due to a strong supersaturation, the chemical composi- yields a hard and a soft fraction, which are called stearin and tion of the crystals is changed compared to crystals formed olein, respectively. under slow kinetic conditions. This study shows to what extent Dry fractionation consists of two steps, a partial crystal- controlled temperature and supercooling during milk fat crys- lization of triacylglycerols from a melt and a subsequent sep- tallization influence crystal amount and the physical properties aration. The resulting differences in the fractions depend on of the resulting fractions. Differences of the thermal characteris- the process characteristics and parameter settings. The effi- tics of the crystal suspensions are directly detected by differen- ciency of separation of the liquid (olein) from the crystalline tial scanning calorimetry and nuclear magnetic resonance. At phase (stearin) influences the quality of the solid fraction to a slow crystallization kinetics, the melting temperature range of great extent. The more liquid is removed, the greater are the the crystals in the suspensions is broader, and the resolution of the melting peak is higher. It is shown that compound crystals differences in the solid fraction, compared to the original milk are formed when supercooling is performed, even if the super- fat (7,9). The crystallization step has a greater influence on cooling takes place only for a short period of time. Controlled the chemical composition of the pure fractions. temperature conditions during crystallization govern larger dif- Crystallization in general can be divided into two charac- ferences in the fatty acid and triacylglycerol composition of the teristic process steps: nucleation and growth. To crystallize a liquid and of the crystalline phases, compared to fractions crys- fat compound, supersaturation or supercooling is necessary. tallized under supercooling conditions, which contain a high This is the driving force for both crystallization steps (10). amount of compound crystals. For fat systems, crystallization is complex because natural JAOCS 75, 897–904 (1998). fats are a mixture of various triacylglycerols. Consequently, the concentration of each triacylglycerol is low and, for ex- KEY WORDS: Compound crystals, crystallization, differential ample, increased supercooling is needed to achieve nucle- scanning calorimetry, fractionation, milk fat, mixed crystals, nu- clear magnetic resonance, polymorphism, process control, tri- ation of this low concentrated species. acylglycerol composition. Furthermore, triacylglycerols are characterized by a com- plex melting behavior. They can solidify in three different crystal structures (α, β′, β) (polymorphism). Different crystal grid structures result depending on the magnitude of the Milk fat has a heterogeneous nature. It contains a large vari- driving force of crystallization. Less stable modifications re- ety of fatty acids with different chainlengths. So far, over 400 quire a lower driving force. The different polymorphic modi- different fatty acids have been identified in milk fat (1–3). fications have different thermodynamic stability, and the The triacylglycerol composition is even more complex be- metastable polymorphic modifications (α, β′) are transformed cause the theoretical number of possible combinations of with time to the stable β form. these fatty acids in triacylglycerols is 4003. Due to its com- In a multicomponent fat, such as milk fat, compound crys- plex composition, the melting range of milk fat is broad and tals can easily be formed due to the low supersaturation of *To whom correspondence should be addressed. one triacylglycerol (11). Compound or mixed crystals are E-mail: [email protected] composed of different molecular species, favored by similar Copyright © 1998 by AOCS Press 897 JAOCS, Vol. 75, no. 8 (1998) 898 B. BREITSCHUH AND E.J. WINDHAB chainlength of the fatty acids (12). Preferably, they form suspensions (created in the rheometer) were filtered 15 min at metastable modifications because the crystal lattice is not 1.5 bar, and the filter medium used was Nybolt PA 1/1/C very dense. Compound crystals cause a narrow melting range (Sefar Inc., Heiden, Switzerland) with a pore size of 1 µm. and a higher crystal fraction (13); furthermore, unstable poly- Calorimetric measurements. The calorimeter used was morphic forms (α, β′) may persist almost indefinitely. a DSC Gold+ (Rheometric Scientific GmbH, Bensheim, Due to its complex composition, the crystallization of tria- Germany) with an accuracy of 1 µW. Gallium [h = 18.95 cal/g, cylglycerols in milk fat and milk fat fractions is not well T (melting) = 29.765°C] was used for temperature and en- known (14). If the temperature is gradually decreased, suc- thalpy calibration, and the instrument was calibrated at cessive crystallization of triacylglycerols occurs. The param- 10°C/min. Aluminum pans were used, and the sample weight eters that influence crystallization and the properties of the was about 1–5 mg. One drop of a crystal suspension was in- final fractions consist of the degree of supercooling, tempera- serted into an empty pan and immediately (within seconds) ture, and residence time. measured at a constant heating rate of 10°C/min, registering The aim of this study is to determine the effect of crystal- the heating curve. As a reference, an empty pan was measured lization temperature and supercooling on the physical and at the same time. For analysis of the heat of fusion, the area chemical characteristics of the resulting milk fat fractions. between the heat flow curve and the extrapolated baseline was The investigations are based on direct measurements of the determined. The cooling was performed by using liquid nitro- calorimetric properties of a crystal suspension, thus detecting gen as refrigerant. Further details are provided elsewhere (16). crystal temperature memory as well as the crystal amount in Nuclear magnetic resonance. The instrument used in these a suspension. investigations was a Minispec NMS 120 (Spectrospin, Bruker Analytical and Medical Instruments, Fällanden, Switzerland). The solid fat content was measured directly from the crystal MATERIALS AND METHODS suspensions (16). Sample. Anhydrous milk fat was obtained from Aargauer Zen- Gas chromatography. The fatty acid composition was de- tralmolkerei Suhr (Suhr, Switzerland). The melting point of termined as methyl esters by gas chromatography (HP 6890, the milk fat was 35°C [corresponding to less than 1.5% solid FID, Hewlett-Packard, Basel, Switzerland) on an SGE BPX- fat content measured by nuclear magnetic resonance (NMR) 70 (Infochroma, Zug, Switzerland) column. The triacylglyc- (15)]. The fatty acid composition of the milk fat is given in erol composition was analyzed in a gas chromatograph (HP Table 1, and the triacylglycerol composition is given in 6890) with an apolar column (J&W DB-5HT, MSP Friedi, Table 2. Koeniz, Switzerland). The fat was diluted in heptane. The re- Standardized preparation of crystal suspensions. The milk sults are expressed as mean average weight percentages on a fat was crystallized in a rheometer (Bohlin Visco 88; Bohlin fatty acid or triacylglycerol basis, respectively (17–19). Instruments Inc., Cranbury NJ; Searle principle) at defined temperatures and a constant shear rate of 1041 s−1 until an RESULTS equilibrium state was reached. Further information is pro- vided elsewhere (16). Crystallization kinetics. Because milk fat is a multicompo- Separation into milk fat fractions. To analyze the resulting nent fat, the amount of triacylglycerols that crystallizes is fractions, the crystal suspensions were filtered in a pressure mainly dependent on the crystallization temperature. In a filter (BHS, Sonthofen, Germany). The equilibrated crystal rheometer for reproducible simulation of a crystallization TABLE 1 Fatty Acid Composition of Milk Fat and Separated Suspensions Crystallized in a Rheometer Directly at Fractionation Temperaturea