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dc.creatorLin, Lanen_US
dc.date.accessioned2012-06-07T22:49:30Z
dc.date.available2012-06-07T22:49:30Z
dc.date.created1997en_US
dc.date.issued1997
dc.identifier.urihttp://hdl.handle.net/1969.1/ETD-TAMU-1997-THESIS-L56en_US
dc.descriptionDue to the character of the original source materials and the nature of batch digitization, quality control issues may be present in this document. Please report any quality issues you encounter to digital@library.tamu.edu, referencing the URI of the item.en_US
dc.descriptionIncludes bibliographical references.en_US
dc.descriptionIssued also on microfiche from Lange Micrographics.en_US
dc.description.abstractCrude vegetable oils contain various minor substances like phospholipids, coloring pigments, and free fatty acids (FFA) that may affect quality of the oil. Reduction of energy costs and waste disposal are major concerns for many oil refiners who are looking for alternative methods to improve conventional refining methods. During the last decade, energy efficient membrane separation technology has evolved dramatically. This thesis reports a study on degumming crude vegetable oil using membrane separation. In the bench-scale study, two membranes were evaluated for their flux and rejection properties. Process parameters including pressure, temperature, feed velocity and volumetric concentration factor were examined. A 99.6% rejection of phospholipids and a flux of 22.4 LMH were achieved at pressure 300 psi, temperature 40'C and feed velocity 220 1/hr using DS-7 membrane, and significant reduction of the coloring pigments was observed as well. In the pilot-scale study, the spiral wound DS-7 membrane was found effective for 100% rejection of phospholipids with a permeate flux of 57.6 LMH. The rejection rates of phospholipids, Mg and Ca were 100%, 99.6% and 54.6%, respectively. Resistance-in-series model of the membrane system was also studied. The membrane resistance, the fouling resistance, and the polarization resistance for the pilotscale system were 0.29, 0.043, and 4.49, respectively. Evaluation on membrane fouling and cleaning showed that flux decreased rapidly during the first several hours and membrane cleaning presented no significant problem. The pilot-scale study confirmed results of the bench-scale system and provides useful data for commercializing membrane refining process in the near future. KEY WORDS: Membrane separation, crude vegetable oil, degumming, phospholipids.en_US
dc.format.mediumelectronicen_US
dc.format.mimetypeapplication/pdfen_US
dc.language.isoen_USen_US
dc.publisherTexas A&M Universityen_US
dc.rightsThis thesis was part of a retrospective digitization project authorized by the Texas A&M University Libraries in 2008. Copyright remains vested with the author(s). It is the user's responsibility to secure permission from the copyright holder(s) for re-use of the work beyond the provision of Fair Use.en_US
dc.subjectfood science and technology.en_US
dc.subjectMajor food science and technology.en_US
dc.titleMembrane degumming of crude vegetable oilen_US
dc.typeThesisen_US
thesis.degree.disciplinefood science and technologyen_US
thesis.degree.nameM.S.en_US
thesis.degree.levelMastersen_US
dc.type.genrethesis
dc.type.materialtexten_US
dc.format.digitalOriginreformatted digitalen_US


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