Palm stearin with a melting point (m.p.) of 49.8°C was fractionated from acetone to produce a low-melting palm stearin (m.p. = 35°C) and a higher-melting palm stearin (HMPS, m.p. = 58°C) fraction. HMPS was modified by interesterification with 60% (by weight) of individual liquid oils from sunflower, soybean, and rice bran by means of Mucor miehei lipase. The interesterified products were evaluated for m.p., solid fat content, and carbon number glyceride composition. When HMPS was interesterified individually with sunflower, soybean or rice bran at the 60% level, the m.p. of the interesterified products were 37.5, 38.9, and 39.6°C, respectively. The solid fat content of the interesterified products were 30-35 at 10°C, 17-19 at 20°C, and 6-10 at 30°C, respectively. The carbon number glyceride compositions also changed significantly. C 48 and C 54 glycerides decreased remarkably with a corresponding increase of the C 50 and C 52 glycerides. All these interesterified products were suitable for use as trans acid-free and polyunsaturated fatty acid-rich shortening and margarine fat bases. JAOCS 74, 589-592 (1997).
KEY WORDS:High-melting palm stearin, low-melting palm stearin, Mucor miehei lipase, palm stearin.Palm stearins, produced in commerce from palm oil by fractionation, have limited use due to their high melting points. A great deal of work has already been done in utilizing palm stearin by interesterification and by blending in mixtures with liquid oils (1). Nutritional quality of these interesterified products (2) and blended products (3) has also been evaluated.Palm stearin can be further fractionated (4) to produce a low-melting palm stearin (LMPS) and a higher-melting palm stearin (HMPS). The LMPS fraction of melting point 35°C will be more useful than palm stearin as such. The HMPS fraction with melting point of about 58°C cannot be used as such in fat-based edible products due to its high melting point. However, HMPS can be used after some modification by lipase-catalyzed interesterification with other liquid oils.The present study aims at utilizing HMPS by lipase-catalyzed interesterification with individual liquid oils, such as from sunflower, soybean and rice bran, to produce fatty materials suitable for the production of trans-free shortening and margarine.
MATERIALS AND METHODS
Refined, bleached, and deodorized (RBD) palm stearin was provided by PORIM (Kuala Lumpur, Malaysia). RBD sunflower oil was supplied by ITC (Agro-Tech) Ltd. (Hyderabad, India); RBD soybean oil and rice bran oil were supplied by K.N. Oil Industries (Raipur, India). 1,3-Specific Mucor miehei lipase was a kind gift of NOVO Industry (A/S Copenhagen, Denmark). Except otherwise specified, all other chemicals and solvents (A.R. Grade) were purchased from S.D. Fine Chemicals (Calcutta, India).Fractionation of palm stearin. Palm stearin was fractionated from acetone (5 mL/g palm stearin) at 35°C for 3 h to get 19% by weight of HMPS and 81% by weight of LMPS. These two fractions were collected after removal of acetone.Lipase-catalyzed int...