{"id":{"repo_id":"uiuc","oai_identifier":"oai:www.ideals.illinois.edu:2142/86087"},"canonical_url":"https://search.dev.ndltd.org/etd/uiuc/oai:www.ideals.illinois.edu:2142/86087","repository":{"repo_id":"uiuc","name":"University of Illinois - Urbana-Champaign","base_url":"https://www.ideals.illinois.edu/oai-pmh"},"display":{"title":"Microfiltration of Corn Starch Hydrolysate Using Ceramic Membranes","abstract":"A microfiltration membrane plant was designed for clarification of 500 gallons per minute (113.6 m$\\sp3$/hour) of corn starch hydrolysate based on the process model and various capital and operating costs. The optimum membrane plant would have two feed-and-bleed stages with a total area of 883.2 m$\\sp2,$ both stages having equal area. Total capital cost of the ceramic membrane plant, including CIP (clean-in-place) system would be $2.08 million, with operating costs of \\$517,408/year. In contrast, operating costs for rotary vacuum precoat filtration, which uses diatomaceous earth as a filter aid, would be $1.8 million per year.","abstract_html":"A microfiltration membrane plant was designed for clarification of 500 gallons per minute (113.6 m$\\sp3$/hour) of corn starch hydrolysate based on the process model and various capital and operating costs. The optimum membrane plant would have two feed-and-bleed stages with a total area of 883.2 m$\\sp2,$ both stages having equal area. Total capital cost of the ceramic membrane plant, including CIP (clean-in-place) system would be $2.08 million, with operating costs of \\$517,408/year. In contrast, operating costs for rotary vacuum precoat filtration, which uses diatomaceous earth as a filter aid, would be $1.8 million per year.","abstract_has_math":true,"creators":["Singh, Navpreet"],"institution":"University of Illinois at Urbana-Champaign","degree_name":"Ph.D.","degree_level":"Dissertation","degree_discipline":"Agricultural Engineering","degree_department":null,"school":null,"contributors":["Cheryan, Munir"],"advisors":[],"committee_chairs":[],"committee_members":[],"year":null,"date_issued":"10000-01-01","date_published":"10000-01-01","updated_at":"2026-07-22T22:26:26Z","subjects":["Agriculture, Food Science and Technology"],"languages":["eng"],"rights":[],"rights_urls":[],"identifier_entries":[{"key":"dc:identifier","label":"Identifier","values":["(MiAaPQ)AAI9812774"],"render_values":[{"text":"(MiAaPQ)AAI9812774","href":null,"code":true}]}]},"links":{"outbound_url":"http://hdl.handle.net/2142/86087","outbound_label":"Handle","outbound_source":"dc:identifier"},"metadata_groups":[{"id":"people","label":"People","entries":[{"key":"dc:contributor","label":"Contributor","values":["Cheryan, Munir"]},{"key":"dc:creator","label":"Author","values":["Singh, Navpreet"]}]},{"id":"academic_context","label":"Academic Context","entries":[{"key":"dc:date","label":"Dc Date","values":["10000-01-01","1997","2015-09-28T14:53:54Z"]},{"key":"dc:type","label":"Dc Type","values":["text"]},{"key":"thesis:degree_discipline","label":"Discipline","values":["Agricultural Engineering"]},{"key":"thesis:degree_level","label":"Degree Level","values":["Dissertation"]},{"key":"thesis:degree_name","label":"Degree Name","values":["Ph.D."]},{"key":"thesis:institution_name","label":"Thesis Institution Name","values":["University of Illinois at Urbana-Champaign"]}]},{"id":"subjects_keywords","label":"Subjects and Keywords","entries":[{"key":"dc:subject","label":"Dc Subject","values":["Agriculture, Food Science and Technology"]}]},{"id":"language_rights","label":"Language and Rights","entries":[{"key":"dc:language","label":"Dc Language","values":["eng"]}]},{"id":"identifiers","label":"Identifiers","entries":[{"key":"dc:identifier","label":"Identifier","values":["http://hdl.handle.net/2142/86087","(MiAaPQ)AAI9812774"]}]},{"id":"additional","label":"Additional Metadata","entries":[{"key":"dc:description","label":"Description","values":["A microfiltration membrane plant was designed for clarification of 500 gallons per minute (113.6 m$\\sp3$/hour) of corn starch hydrolysate based on the process model and various capital and operating costs. The optimum membrane plant would have two feed-and-bleed stages with a total area of 883.2 m$\\sp2,$ both stages having equal area. Total capital cost of the ceramic membrane plant, including CIP (clean-in-place) system would be $2.08 million, with operating costs of \\$517,408/year. In contrast, operating costs for rotary vacuum precoat filtration, which uses diatomaceous earth as a filter aid, would be $1.8 million per year.","Made available in DSpace on 2015-09-28T14:53:54Z (GMT). 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The optimum membrane plant would have two feed-and-bleed stages with a total area of 883.2 m$\\sp2,$ both stages having equal area. Total capital cost of the ceramic membrane plant, including CIP (clean-in-place) system would be $2.08 million, with operating costs of \\$517,408/year. In contrast, operating costs for rotary vacuum precoat filtration, which uses diatomaceous earth as a filter aid, would be $1.8 million per year.","Made available in DSpace on 2015-09-28T14:53:54Z (GMT). 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