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作者机构:Department of Food Engineering URI-Campus de Erechim Av. Sete de Setembro 1621 Erechim 99700-000 RS Brazil Program of Chemical Engineering COPPE UFRJ-Centro de Tecnologia Bloco G Sala 115 Rio de Janeiro 21941-972 R JBrazil
出 版 物:《Journal of Food Science and Engineering》 (食品科学与工程(英文版)(美国))
年 卷 期:2012年第2卷第11期
页 面:616-624页
学科分类:081704[工学-应用化学] 07[理学] 08[工学] 0817[工学-化学工程与技术] 081701[工学-化学工程] 070303[理学-有机化学] 0703[理学-化学]
主 题:Soybean oil n-hexane ultrafiltration nanofiltration polymeric membranes.
摘 要:Separation of refined soybean oil/n-hexane miscellas was studied using different commercial ultra- and nanofiltration membranes, with cut-oil's in the range of 1 to 5 kDa and salt rejection higher than 97% (MgSO4). Commercial soybean oil and n-hexane miscellas with 1:3 and 1:1 mass ratios were permeated in a dead-end module. The effects of the feed pressure (2-25 bar) on oil and n-hexane fluxes and rejection were investigated. Oil rejection ranged from negative values to 30.8%, soybean oil flux from 28.9 to 617.8 g/m2 hl and n-hexane flux from 8.5 to 1,078.5 g m2 hl. Membrane fouling was observed at all experimental conditions studied. The membrane separation process has proven to be a promising alternative to solvent recovery in soybean oil extraction.