The effect of cooling rate on the degree of removal of saturated acyl groups from FFA derived from canola oil and the isolation of di-and polyunsaturated acyl groups from FFA derived from vegetable and fish oil, respectively, during urea inclusion compound (UIC)-based fractionation was investigated. Traditionally, slow cooling has been used (ca. −1°C min −1 ). A more rapid cooling rate (−47°C min −1 ) produced UIC crystals of similar morphology and thermodynamic properties, but of a size an order of magnitude smaller than the UIC formed during slow cooling. Fractionations used only renewable materials (urea, FFA, and 95% ethanol as solvent) and benign operating conditions (ambient pressure, 25-75°C, and neutral pH). When the recovery of FFA (in the solvent-rich phase) was relatively high (>60%), the selectivity of UIC-based fractionation toward the inclusion of saturated FFA and against polyunsaturated FFA was not affected by the cooling rate. In contrast, when the FFA recovery was low, representing cases in which an increase of the PUFA purity is a more important economic goal, a slower cooling rate resulted in a significantly greater discrimination against PUFA groups, hence to a FFA product with a measurably greater purity. Paper no. J11191 in JAOCS 82, 253-259 (March 2006). KEY WORDS: Canola oil, DHA (docosahexaenoic acid), DSC, EPA (eicosapentaenoic acid), FFA (fractionation of), fish oil, PUFA, urea inclusion compounds, vegetable oil.Urea inclusion compounds (UIC), hexagonal clanthrate materials consisting of hydrogen-bonded networks of urea that form a series of linear, parallel, narrow channels of diameter 0.55-0.58 nm, are well-known vehicles for fractionating or purifying FFA or FAME (reviewed in Ref. 1). For a given mixture of FFA or FAME, UIC will selectively remove long-chain saturated acyl groups, while acyl groups with branching and polyunsaturation do not partition as strongly to the UIC solid phase. Thus, UIC have been used to isolate PUFA from FFA derived from fish, linseed, and borage oils and to remove saturated acyl groups from FFA derived from edible oils such as low erucic acid rapeseed (LEAR) (reviewed in Refs. 2-4). UIC-based fractionation has potential value as a large-scale and robust prefractionation step because of its low temperature and environmentally friendly operating conditions, and its use of inexpensive renewable materials (urea and ethanol or methanol as solvent). To be a viable choice, a process that uses UIC-based fractionation must occur within a short time period. In contrast, a typical UIC-based fractionation procedure consists of slowly cooling a homogeneous solution of urea, FFA, and solvent for several hours. Recently, however, a rapid cooling process effectively fractionated FFA in a highly reproducible fashion, resulting in a simple and scalable purification process (5,6). But, as suggested recently by Lee (7), the use of a slower-temperature cooling program improves the selectivity by reducing the amount of tetragonal crystals of pure urea that form. The purpose of...