Pecan Oil Recovery and Composition as Affected by Temperature, Pressure, and Supercritical CO2 Flow Rate |
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Authors: | W.S. ALEXANDER G.H. BRUSEWITZ N.O. MANESS |
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Affiliation: | Authors Alexander and Brusewitz are with the Biosystems &Agricultural Engineering Dept., 216 Ag Hall, Stillwater, OK 74078. Author Maness is with the Dept. of Horticulture &Landscape Architecture, Oklahoma State Univ., Stillwater, OK 74078. Address inquiries to Dr. G.H. Brusewitz. |
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Abstract: | Effects of supercritical CO2 flow rate, extraction temperature, and pressure were studied on oil recovery, fatty acid composition, and factors that control solute extraction from intact pecan halves. After an initial solubility dominant period, extraction was influenced by diffusion of oil from within the pecan. The effective diffusion coefficient was 9.76 × 10-12 m2/s. In the first 105 min, more oil was extracted as CO2 flow increased from 1.0 to 7.5 standard L/min (slpm). Beyond 120 min, increasing CO2 flow from 4 to 7.5 slpm produced negligible differences in amounts of extracted oil. At 2.5 slpm CO2 flow and 45–75°C, the oil extracted increased by 60% when pressure increased from 41.3 to 55.1 MPa and yielded slightly more at 66.8 MPa. Temperature, pressure, micrometering valve temperature, cultivar (but not extraction time) affected fatty acid (palmitic, stearic, oleic, linoleic, and linolenic) composition of pecan oil. |
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Keywords: | supercritical CO2 oil extraction pecan diffusion coefficient |
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