With the use of two central composite designs, the effects of agitation rate, fractionation temperature, and residence time on the thermal properties of the stearin and olein milk fat fractions were investigated. The main function of agitation during fat fractionation was suspending the crystal aggregates and enhancing the heat transfer. For the experimental conditions described here, crystal aggregation did not seem to be affected by agitation. The effect of fractionation temperature on the physical properties of the olein fraction was very significant. Triangle diagrams were shown to be a useful tool for monitoring and designing fractionation processes. They illustrate that oleins with similar melting properties can be produced over a range of yields of stearin, which is important from an industrial point of view. Crystallizer residence time, which influences production costs, clearly affects both stearin yield and olein melting properties. For any fractionation temperature, stearin fractions with virtually identical melting properties and yields can be obtained over a range of olein melting properties. Manipulation of both the fractionation temperature and residence time allows the fractionation process to be adapted to meet changing market demands for fractions with different melting properties.The production of anhydrous milk fat (AMF) was a conservation method for the large stocks of butter produced during the 1980s in the European Community. By removing the water phase from butter, milk fat could be stored for several years without significant loss of quality. Nowadays, AMF is used in the confectionery, bakery, and ice cream industries for its sensorial properties and its marketing value as a natural ingredient. New techniques such as fractionation, texturization, and recombination have led to new applications for AMF, especially in puff pastry and cold spreadable fat blends. These processes are used to improve product quality.Fractionation is a separation process by which the fat is divided into different fractions, each having its own physical and chemical properties. Two types of fractionation exist: dry (or melt) fractionation and solvent fractionation (1). The latter is never used on an industrial scale for milk fat owing to flavor loss but is extensively used in vegetable oil processing, e.g., for the production of cocoa butter substitutes. In dry fractionation, crystals are formed by controlled cooling and agitation. The crystals in suspension are then separated on a rotary drum belt filter, a filter press, a centrifuge, or by means of an emulsifier followed by a centrifugation step. Fractionation of AMF was extensively reviewed by Kaylegian and Lindsay (2) and more briefly by Deffense (3).The effects of process parameters such as agitation rate, cooling rate, and fractionation temperature have been investigated several times. Deffense (4) discussed four factors that influence crystallization of milk fat during fractionation: oil composition, polymorphism, rate of cooling, and intersolubility. In ad...