Effects of Vegetable Oil Type and Lipophilic Emulsifiers on the Induction Period of Fat Crystallization

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1 Journal of Oleo Science Copyright 2015 by Japan Oil Chemists Society doi : /jos.ess15170 Effects of Vegetable Oil Type and Lipophilic Emulsifiers on the Induction Period of Fat Crystallization Yayoi Miyagawa 1, Takenobu Ogawa 2, Kyuya Nakagawa 1 and Shuji Adachi 1* 1 Division of Food Science and Biotechnology, Graduate School of Agriculture, Kyoto University (Sakyo-ku, Kyoto , JAPAN) 2 Division of Agronomy and Horticultural Science, Graduate School of Agriculture, Kyoto University (Gokasho, Uji, Kyoto , JAPAN) Abstract: The induction period of crystallization, which is defined as the time required for oil to start to crystallize, is useful indicator of the freeze-thaw stability of food emulsions such as mayonnaise. We investigated the induction period of vegetable oils with low melting points, such as rapeseed and soybean oils, which are commonly employed for mayonnaise production. The induction period was measured by monitoring the temperature of a specimen during storage at low temperature. The induction period depended on the type of oil and lipophilic emulsifier, emulsifier concentration, and storage temperature. The effect of the oil type on the induction period depended on the composition of the oil. Differential scanning calorimetry (DSC) analyses of the lipophilic emulsifiers suggested that the melting trend of the emulsifier is strongly related to the induction period. Key words: crystallization, induction period, low-melting point, rapeseed oil, soybean oil 1 INTRODUCTION Fats and oils are common components of food products, and they are strongly related to the physicochemical properties and stability of these products. In the case of butter and chocolate production, for instance, the crystallization characteristics of fats and oils, which are the continuous phase of the water-in-oil W/O emulsion, affect the texture and appearance of the product, and product qualities can be manipulated by controlling fat crystallization during processing 1, 2. In the case of fresh cream and mayonnaise, which are O/W emulsions, product quality is strongly linked to emulsion stability. Coalescence of the oil droplets or phase separation during processing and storage cause demulsification, which leads to serious quality loss. Demulsification of food products is closely related to fat crystallization 3, 4 ; accordingly, food engineers aim to control fat crystallization. Many studies have focused on fat crystallization, especially on the crystallization of tripalmitin 5, 6, n- hexadecane 7 9, palm oil 10 14, and confectionary-coating fat 8, 15, which have high melting points and have a single component or are composed of relatively few types of fatty acids. However, few studies have examined vegetable oils with low melting points, and their crystallization induction periods have scarcely been reported. Here, the induction period is defined as the time duration for oil to start to crystallize during storage at a certain temperature. In our preliminary experiments, the induction period of fat crystallization in mayonnaise was measured during storage at 20 to 40. After a certain period at each storage temperature, a temperature raise due to crystallization of the rapeseed oil in mayonnaise was observed, and the mayonnaise was consequently demulsified. The induction periods varied between 15 min and 6 h, depending on the storage temperature, and the induction periods were observed with high repeatability. These results showed that the induction period of crystallization could be used as an indicator of the freeze-thaw stability of food emulsions such as mayonnaise. In this study, we investigated the induction period of vegetable oils with low melting points, such as rapeseed and soybean oils, which are usually used in mayonnaise, during storage at low temperatures. The effects of lipophilic emulsifiers that are used commercially to inhibit, promote, or regulate the crystallization behavior of oil on the induction period of crystallization were also investigated. 2 EXPERIMENTAL 2.1 Materials Rapeseed and soybean oils were purchased from Wako * Correspondence to: Shuji Adachi, Division of Food Science and Biotechnology, Graduate School of Agriculture, Kyoto University (Sakyo-ku, Kyoto , JAPAN) adachi@kais.kyoto-u.ac.jp Accepted August 26, 2015 (received for review July 15, 2015) Journal of Oleo Science ISSN print / ISSN online

2 Y. Miyagawa, T. Ogawa and K. Nakagawa et al. Pure Chemical Industries Osaka, Japan. Six types of lipophilic emulsifiers were used: decaglyceryl docosanoic acid ester, which promotes crystallization and is denoted LE A Mitsubishi Kagaku Food Corporation, Tokyo, Japan, hexaglyceryl octa-stearic acid ester LE B, which coordinates crystal size Taiyo Kagaku, Tokyo, Japan, glycerol fatty acid ester LE E, which inhibits crystallization Taiyo Kagaku, glycerol mono-stearic acid ester LE C Kao Corp., Tokyo, Japan, and decaglyceryl mono-stearate ester LE D and decaglyceryl fatty acid ester LE F, which inhibit crystallization Sakamoto Yakuhin Kogyo, Osaka, Japan. 2.2 Temperature measurement of the vegetable oils during storage Changes in temperature during storage were measured for rapeseed oil, soybean oil, and their mixtures at 3:1, 2:2, and 1:3 ratios by weight. A glass tube φ18 mm 90 mm was filled with an oil sample, and the ends of the tube were tightly capped with silicone rubber stoppers. A thermocouple AD 1214; A & D Company, Tokyo, Japan was installed at the center of the tube and fixed with a phenol resin Fig. 1. The sample was pre-heated at 30 for approximately 1 h in an air oven DO 300FA, As One, Osaka, Japan and then placed in low-temperature conditions with a thermostat SU 261, Espec, Osaka, Japan set at 20 to 50. The temperature of the specimen was monitored at 20-s intervals. To examine the effect of a lipophilic emulsifier on the temperature change of oil, a given amount of the emulsifier was mixed with g of rapeseed oil in a 100-mL beaker and stirred for approximately 30 min at 80 in an air oven DN 44; Yamato, Tokyo, Japan to melt and disperse the emulsifier. After the solution was equilibrated at 30 in the oven for approximately 1 h, the temperature measurement was carried following the same methods described above. 2.3 Measurement of the melting point of the lipophilic emulsifiers The melting point of an emulsifier was measured by differential scanning calorimetry DSC; DSC7020; Hitachi High Tech Science Corporation, Japan. The melting points of the emulsifiers LE A, LE B, LE C, and LE D were measured as received, whereas those of LE E and LE F were measured after melting and homogenizing in a water bath at 70. Approximately 5 mg of the emulsifier was enclosed in an Alodine-coated aluminum cell. An empty cell was employed as the reference. After holding the sample at 20 for 10 min, the temperature was raised to 80 at a rate of 2 /min, and held at 80 for 10 min. The melt was cooled to 60 at a rate of 2 /min, held at 60 for 10 min, and then raised again to 80 at 2 / min. Fig. 1 Equipment for temperature measurement of the vegetable oils during storage. 3 RESULTS AND DISCUSSION 3.1 Effects of oil type and oil mixing ratio on induction period Temperature profiles of rapeseed oil during storage at 15 to 40 are shown in Fig. 2. A temperature rise due to heat generation was observed after a certain induction period 10 min to 15 h for each storage temperature. The induction period was determined as the time from the beginning of storage to the point where the temperature started to rise due to heat generation. The induction period was shortened by lowering the storage temperature, except for storage temperature between 21 and 25. In the temperature range, the induction periods were 8 12 h, which were longer than that at 20. The profiles obtained for storage at 21, 23 and 25 were unique, namely, the peaks were obviously broader than those observed at other storage temperatures. When the storage temperature was set at below 35, crystallization was induced before the storage temperature was reached. When soybean oil was employed, the oil became cloudy and opaque under storage at 20 for about 2 weeks. This color change is consistent with oil crystallization, but a temperature rise was not observed when stored at 20 to 25. In the present experimental set-up, the 1170

3 Induction period of fat crystallization of vegetable oils Fig. 2 Temperature profile of rapeseed oil during storage at -15 to -40. Inset: initial temperature profile during storage at -35 and -40. observed temperature rise was the consequence of a balance between heat generation due to crystallization and heat loss to the environment. The shape and strength of the peaks do not always correspond to the total amount of heat generated, but to the rate of heat generation. Therefore, the appearance of broad peaks suggested that the duration of crystallization was rather long with gradual continued heat generation. The vegetable oil consists of many kind of acylglycerols with different melting points. The shape variation of the peaks could be ascribed to differences in the component and its structure of crystallized acylglycerols. Additional studies are necessary, however, to clarify this point. The induction periods of rapeseed oil, soybean oil, and their mixtures were plotted as a function of storage temperature Fig. 3. For the mixed oils, the induction periods at 25 were prolonged similar to that of rapeseed oil, and this trend was more apparent when the ratio of soybean oil to rapeseed oil was decreased. The induction period of rapeseed oil was shorter than that of soybean oil at all storage temperatures. The period would be affected by the degree of unsaturation in a whole oil and the molecular structures of acylglycerols. The major components in rapeseed and soybean oils are oleic and linoleic acids, respectively, and the melting point of oleic acid is higher than that of linoleic acid 16. Because the induction period depends on the composition of the oils with different melting points, the induction periods of the mixed oils were determined by the ratio of rapeseed oil to soybean oil. Fig. 3 Induction period of rapeseed oil, soybean oil, and their mixtures during storage at -15 to -50. : rapeseed oil, : mixture of rapeseed and soybean oils at a 3:1 ratio by weight, : mixture at 1:1, : mixture at 1:3, : soybean oil. 3.2 Effect of the lipophilic emulsifier The induction periods of crystallization for rapeseed oil with and kg/kg-oil lipophilic emulsifiers are shown in Fig. 4. At each storage temperature, the induction periods were slightly different from those of rapeseed oil without any emulsifier control. When kg/kg-oil emulsifiers LE A a promoter, LE B a regulator, LF E an inhibitor, and LE F an inhibitor, were added to the rapeseed oil, the induction period were changed but no tendency was observed. When kg/kg-oil emulsifiers LE A, LE B, LF E, and LE F, were added, the induction periods at 15 and 20 were largely prolonged by LE E and LE F, slightly shortened by LE A, and not significantly altered by LE B. These results showed that the promoter shortens the induction period and the inhibitor prolongs it. However, no effects of LE E and LE F were observed when stored at 25. Interestingly, for storage at below 30, all of the emulsifiers resulted in shorter induction periods than that of the control. This suggests that the emulsifier had different roles in crystallization depending on the temperature. The fatty acid moiety of the emulsifier acts as a crystal nucleus to promote crystallization 9, 12. This finding suggested that the fatty acid moiety did not act as crystal nucleus owing to the lack of solidification at 15 and 20, but the moiety provided a solid surface as a nucleus at temperatures of 30 and lower. Figure 5 shows the DSC curves for the emulsifiers. From 1171

4 Y. Miyagawa, T. Ogawa and K. Nakagawa et al. Fig. 4 Effect of the emulsifiers on the induction period of rapeseed oil during storage at -15 to -40. (A) kg/kg-oil addition, (B) kg/kg-oil addition. : rapeseed oil, : LE A, : LE B, : LE C, : LE D, : LE E, : LE F. each DSC curve, peak temperature T p and onset temperature T o were determined. The emulsifier LE A, which shortened the induction period, showed a sharp endothermic peak T o 65.7 and T p 69.9, and LE B, which had no effect on the induction period above 20, also showed a sharp peak T o 55.1 and T p In contrast, the peaks due to the melting of LE E and LE F appeared at lower temperatures and were broad in shape, i.e., T o 10.1 and 0.9, and T p 24.5 and 21.2, respectively. The onset of melting was higher for LE E than LE F. The emulsifiers LE C and LE D, which hardly affected the induction period below 25, showed two sharp peaks for each, and the melting point for LE C was between those of LE B and LE E.The peaks appeared at T o 63.9 and 19.0, and T p 67.8 and One of the sharp peaks for LE D at 3 was ascribed to the melting of ice because the emulsifier includes 60 w/w water, and another peak due to the melting of the fatty acid ester was observed at T o 41.8 and T p These trends in melting support the claim that the fatty acid moiety affects the induction period as a nucleus. The effects of the concentration of the emulsifiers LE A, LE E, and LE F, on the induction periods were studied at 15, 20, and 30 Fig. 6. The induction period was shortened by increasing the LE A concentration for all storage temperatures, except for 0.03 kg/kg-oil additive at 15. At 15 and 20, the induction periods were prolonged by increasing the LE E and LE F concentrations, although they did not depend on the emulsifier concentration at 30. The dependences of the induction periods at 15 and 20 on the LE E concentration Fig. 5 Differential scanning calorimetry (DSC) curves of the emulsifiers.(a) LE A, (b) LE B, (c) LE C, (d) LE D, (e) LE E, (f) LE F. were different from those on the LE F concentrations at concentrations higher than 0.01 kg/kg-oil. However, the 1172

5 Induction period of fat crystallization of vegetable oils Fig. 6 Effect of the concentration of the emulsifiers on the induction period during storage at -15 ( ), -20 ( ), and -30 ( ). (A) LE A, (B) LE E, (C) LE F. trends were similar to those at concentrations lower than 0.01 kg/kg-oil. The shorter induction periods at 15 for 0.03 and 0.05 kg/kg-oil were ascribed to the broader peaks data not shown. When the emulsifier LE F was added at a concentration of 0.05 kg/kg-oil and stored at 20, the majority of the oil was not crystallized on day 14, although it was partially crystallized between the glass tube and the silicon caps, and between the thermocouple and the phenol resin. During storage at 15, the oil did not crystallize at all at the LE F concentration of 0.05 kg/kg-oil, even on day 14, although partial crystallization was also observed at the concentration of 0.03 kg/kg-oil. These results showed that the emulsifier LE F is a promising additive to prolong the induction period at approximately 20. The melting behavior of a lipophilic emulsifier enables us to predict its effect on the induction period of oil, and can be useful in the selection of an appropriate additive to confer tolerance against freezing to an oil with a low melting point, such as rapeseed oil. 4 CONCLUSION The temperature profiles of rapeseed oil, soybean oil, and their mixtures during storage at 15 to 50 were monitored and the induction periods of crystallization of the oils were investigated. The induction periods of the specimens were shorter for lower storage temperatures. The induction periods of the rapeseed oil and its mixtures with soybean oil were longer at 25 than at 20, and this trend was more remarkable for increased ratios of rapeseed oil to soybean oil. The induction periods for rapeseed oils mixed with various lipophilic emulsifiers were also investigated. The addition of an emulsifier significantly affected the induction period when stored at 20 or higher. The emulsifier that could inhibit fat crystallization prolonged the induction period, whereas the promoter shortened it. The effects of the emulsifiers, however, were largely dependent on storage temperature and all emulsifiers shortened the induction period at temperatures below 30. The role of the lipophilic emulsifier on the induction period was strongly related to its melting point. ACKNOWLEDGEMENT This study was carried out during the course of the project The Cereal Science Consortium by Kyoto University, Gifu University, and the Nisshin Seifun Group, Inc., and was supported financially by the group. References 1 Buldo, P.; Wiking, L. The role of mixing temperature on microstructure and rheological properties of butter blends. J. Am. Oil Chem. Soc. 87, Deman, J. M. Consistency of fats: a review. J. Am. Oil Chem. Soc. 60, Rousseau, D. Fat crystal and emulsion stability a review. Food Res. Int. 33, Boode, K.; Walstra, P. Partial coalescence in oil-in-water emulsions 1. Nature of the aggregation. Colloids Surf. A Physicochem. Eng. Asp. 81, Sato, K. Crystallization behavior of fats and lipids a review. Chem. Eng. Sci. 56, Himawan, C.; Starov, V. M.; Stapley, A. G. F. Thermodynamic and kinetic aspects of fat crystallization. Adv. Colloid Interface Sci. 122, Ghosh, S.; Coupland, J. N. Factors affecting the freeze- 1173

6 Y. Miyagawa, T. Ogawa and K. Nakagawa et al. thaw stability of emulsions. Food Hydrocoll. 22, Vanapalli, S. A.; Palanuwech, J.; Coupland, J. N. Stability of emulsions to dispersed phase crystallization: effect of oil type, dispersed phase volume fraction, and cooling rate. Colloids Surf. A Physicochem. Eng. Asp. 204, Sakamoto, M.; Fukunaga, K.; Kuriyama, J.; Sato, K. Retardation effects of polyglycerol fatty acid esters on the crystallization of n-hexadecane. J. Oleo Sci. 54, Campbell, D. S.; Goff, H. D.; Rousseau, D. Comparison of crystallization properties of a palm stearin/canola oil blend and lard in bulk and emulsified form. Food Res. Int. 35, Thanasukarn, P.; Pongsawatmanit, R.; McClements, D. J. Impact of fat and water crystallization on the stability of hydrogenated palm oil-in-water emulsions stabilized by whey protein isolate. Colloids Surf. A Physicochem. Eng. Asp. 246, Sonoda, T.; Takata, Y.; Ueno, S.; Sato, K. Effects of emulsifiers on crystallization behavior of lipid crystals in nanometer-size oil-in-water emulsion droplets. Cryst. Grouth Des. 6, Thanasukarn, P.; Pongsawatmanit, R.; McClements, D.J. Influence of emulsifier type on freeze-thaw stability of hydrogenated palm oil-in-water emulsions. Food Hydrocoll. 18, Cornacchia, L.; Roos, Y. H. Solid-liquid transitions and stability of HPKO-in-water systems emulsified by dairy proteins. Food Biophysics 6, Vanapalli, S. A.; Palanuwech, J.; Coupland, J. N. Influence of fat crystallization on the stability of flocculated emulsions. J. Agric. Food Chem. 50, Ma, F.; Hanna, M. A. Biodiesel production: a review. Bioresour. Technol. 70,

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