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Ultrafiltration optimization for the recovery of β-glucan from oat mill waste
► Ultrafiltration optimized for the recovery of β-glucan (>100 kDa) from oat mill waste. ► Polysulfone showed higher flux recovery than regenerated cellulose and polyethersulfone. ► Cross-flow unit instead of dead-end cell improved performance regarding fouling effect. ► Ultrafiltration performan...
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Published in: | Journal of membrane science 2011-05, Vol.373 (1), p.53-63 |
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creator | Patsioura, Anna Galanakis, Charis M. Gekas, Vassilis |
description | ► Ultrafiltration optimized for the recovery of β-glucan (>100
kDa) from oat mill waste. ► Polysulfone showed higher flux recovery than regenerated cellulose and polyethersulfone. ► Cross-flow unit instead of dead-end cell improved performance regarding fouling effect. ► Ultrafiltration performance was optimum by loading β-glucan concentrations |
doi_str_mv | 10.1016/j.memsci.2011.02.032 |
format | article |
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kDa) from oat mill waste. ► Polysulfone showed higher flux recovery than regenerated cellulose and polyethersulfone. ► Cross-flow unit instead of dead-end cell improved performance regarding fouling effect. ► Ultrafiltration performance was optimum by loading β-glucan concentrations <600
mg/L. ► Membrane disruption was avoided by maintaining transmembrane pressure ≤ 2
bar.
The scope of the current study is to investigate the ultrafiltration process of high molecular weight β-glucan molecules with a final purpose to optimize their recovery from oat mill waste. Therefore, standard β-glucan solutions were processed in a dead-end cell using three types of membranes (regenerated cellulose, polyethersulfone and polysulfone) under several transmembrane pressures. Optimization was conducted by monitoring performance parameters and retention coefficients for each experimental combination. In terms of membrane type, polysulfone was selected as the most appropriate membrane material since it obtained satisfactory retention coefficient and performance parameter values when the β-glucan concentration was less than 600
mg/L. Thereafter, the polysulfone membrane was applied in a pilot cross-flow module instead of a dead-end cell. The retention of β-glucan as well as the flux recovery was markedly improved with no important reduction of the permeate flux. Finally, polysulfone membrane was applied in the pilot cross-flow module for the ultrafiltration of β-glucan containing feeds (<600
mg/L) recovered from the industrial oat mill waste. Results indicated that the optimized ultrafiltration process (polysulfone in cross-flow module, with transmembrane pressure ≤2
bar and β-glucan concentrations
<
600
mg/L) could be utilized in order to recover β-glucan from the oat mill waste feeds and clarify them from smaller organic and inorganic compounds. A disadvantage of the latter application was the small degree of separation between β-glucan and proteins.</description><identifier>ISSN: 0376-7388</identifier><identifier>EISSN: 1873-3123</identifier><identifier>DOI: 10.1016/j.memsci.2011.02.032</identifier><identifier>CODEN: JMESDO</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>artificial membranes ; Beta glucan ; beta-glucans ; cellulose ; Chemistry ; Colloidal state and disperse state ; Dietary fiber ; Exact sciences and technology ; General and physical chemistry ; inorganic compounds ; Macromolecules ; Membranes ; molecular weight ; monitoring ; oats ; Operational features ; Polysaccharides ; proteins ; Ultrafiltration ; wastes</subject><ispartof>Journal of membrane science, 2011-05, Vol.373 (1), p.53-63</ispartof><rights>2011 Elsevier B.V.</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c393t-ed598b252a366823df97a11c8e840798e0f1ca3749e2ac0f43b05014c12d65033</citedby><cites>FETCH-LOGICAL-c393t-ed598b252a366823df97a11c8e840798e0f1ca3749e2ac0f43b05014c12d65033</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27923,27924</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=24099555$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Patsioura, Anna</creatorcontrib><creatorcontrib>Galanakis, Charis M.</creatorcontrib><creatorcontrib>Gekas, Vassilis</creatorcontrib><title>Ultrafiltration optimization for the recovery of β-glucan from oat mill waste</title><title>Journal of membrane science</title><description>► Ultrafiltration optimized for the recovery of β-glucan (>100
kDa) from oat mill waste. ► Polysulfone showed higher flux recovery than regenerated cellulose and polyethersulfone. ► Cross-flow unit instead of dead-end cell improved performance regarding fouling effect. ► Ultrafiltration performance was optimum by loading β-glucan concentrations <600
mg/L. ► Membrane disruption was avoided by maintaining transmembrane pressure ≤ 2
bar.
The scope of the current study is to investigate the ultrafiltration process of high molecular weight β-glucan molecules with a final purpose to optimize their recovery from oat mill waste. Therefore, standard β-glucan solutions were processed in a dead-end cell using three types of membranes (regenerated cellulose, polyethersulfone and polysulfone) under several transmembrane pressures. Optimization was conducted by monitoring performance parameters and retention coefficients for each experimental combination. In terms of membrane type, polysulfone was selected as the most appropriate membrane material since it obtained satisfactory retention coefficient and performance parameter values when the β-glucan concentration was less than 600
mg/L. Thereafter, the polysulfone membrane was applied in a pilot cross-flow module instead of a dead-end cell. The retention of β-glucan as well as the flux recovery was markedly improved with no important reduction of the permeate flux. Finally, polysulfone membrane was applied in the pilot cross-flow module for the ultrafiltration of β-glucan containing feeds (<600
mg/L) recovered from the industrial oat mill waste. Results indicated that the optimized ultrafiltration process (polysulfone in cross-flow module, with transmembrane pressure ≤2
bar and β-glucan concentrations
<
600
mg/L) could be utilized in order to recover β-glucan from the oat mill waste feeds and clarify them from smaller organic and inorganic compounds. A disadvantage of the latter application was the small degree of separation between β-glucan and proteins.</description><subject>artificial membranes</subject><subject>Beta glucan</subject><subject>beta-glucans</subject><subject>cellulose</subject><subject>Chemistry</subject><subject>Colloidal state and disperse state</subject><subject>Dietary fiber</subject><subject>Exact sciences and technology</subject><subject>General and physical chemistry</subject><subject>inorganic compounds</subject><subject>Macromolecules</subject><subject>Membranes</subject><subject>molecular weight</subject><subject>monitoring</subject><subject>oats</subject><subject>Operational features</subject><subject>Polysaccharides</subject><subject>proteins</subject><subject>Ultrafiltration</subject><subject>wastes</subject><issn>0376-7388</issn><issn>1873-3123</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><recordid>eNp9kM9q3DAQh0VIINukb1CIL4Fe7Iwky5YuhRD6D5bk0OxZKPJoo8VebSVtQvpYfZA8U7U49JiLBjHf_Gb4CPlEoaFAu6tNM-GUrG8YUNoAa4CzI7Kgsuc1p4wfkwXwvqt7LuUp-ZDSBoD2INWC3K7GHI3zhzf7sK3CLvvJ_5k_LsQqP2IV0YYnjC9VcNXr33o97q0p3RimKphcTX4cq2eTMp6TE2fGhB_f6hlZfft6f_OjXt59_3lzvawtVzzXOAglH5hghnedZHxwqjeUWomyhV5JBEet4X2rkBkLruUPIIC2lrKhE8D5Gfk85-5i-L3HlPXkk8VxNFsM-6Rp27UCRE9FQdsZtTGkFNHpXfSTiS-agj7o0xs969MHfRqYLvrK2OXbBpOsGV00W-vT_1nWglJCHOIvZs6ZoM06Fmb1qwR1ACCBK1WILzOBRciTx6jLLtxaHHzxmvUQ_Pun_APmYpEI</recordid><startdate>20110501</startdate><enddate>20110501</enddate><creator>Patsioura, Anna</creator><creator>Galanakis, Charis M.</creator><creator>Gekas, Vassilis</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>FBQ</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7UA</scope><scope>C1K</scope><scope>F1W</scope><scope>H97</scope><scope>L.G</scope></search><sort><creationdate>20110501</creationdate><title>Ultrafiltration optimization for the recovery of β-glucan from oat mill waste</title><author>Patsioura, Anna ; Galanakis, Charis M. ; Gekas, Vassilis</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c393t-ed598b252a366823df97a11c8e840798e0f1ca3749e2ac0f43b05014c12d65033</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>artificial membranes</topic><topic>Beta glucan</topic><topic>beta-glucans</topic><topic>cellulose</topic><topic>Chemistry</topic><topic>Colloidal state and disperse state</topic><topic>Dietary fiber</topic><topic>Exact sciences and technology</topic><topic>General and physical chemistry</topic><topic>inorganic compounds</topic><topic>Macromolecules</topic><topic>Membranes</topic><topic>molecular weight</topic><topic>monitoring</topic><topic>oats</topic><topic>Operational features</topic><topic>Polysaccharides</topic><topic>proteins</topic><topic>Ultrafiltration</topic><topic>wastes</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Patsioura, Anna</creatorcontrib><creatorcontrib>Galanakis, Charis M.</creatorcontrib><creatorcontrib>Gekas, Vassilis</creatorcontrib><collection>AGRIS</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Water Resources Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 3: Aquatic Pollution & Environmental Quality</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><jtitle>Journal of membrane science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Patsioura, Anna</au><au>Galanakis, Charis M.</au><au>Gekas, Vassilis</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Ultrafiltration optimization for the recovery of β-glucan from oat mill waste</atitle><jtitle>Journal of membrane science</jtitle><date>2011-05-01</date><risdate>2011</risdate><volume>373</volume><issue>1</issue><spage>53</spage><epage>63</epage><pages>53-63</pages><issn>0376-7388</issn><eissn>1873-3123</eissn><coden>JMESDO</coden><abstract>► Ultrafiltration optimized for the recovery of β-glucan (>100
kDa) from oat mill waste. ► Polysulfone showed higher flux recovery than regenerated cellulose and polyethersulfone. ► Cross-flow unit instead of dead-end cell improved performance regarding fouling effect. ► Ultrafiltration performance was optimum by loading β-glucan concentrations <600
mg/L. ► Membrane disruption was avoided by maintaining transmembrane pressure ≤ 2
bar.
The scope of the current study is to investigate the ultrafiltration process of high molecular weight β-glucan molecules with a final purpose to optimize their recovery from oat mill waste. Therefore, standard β-glucan solutions were processed in a dead-end cell using three types of membranes (regenerated cellulose, polyethersulfone and polysulfone) under several transmembrane pressures. Optimization was conducted by monitoring performance parameters and retention coefficients for each experimental combination. In terms of membrane type, polysulfone was selected as the most appropriate membrane material since it obtained satisfactory retention coefficient and performance parameter values when the β-glucan concentration was less than 600
mg/L. Thereafter, the polysulfone membrane was applied in a pilot cross-flow module instead of a dead-end cell. The retention of β-glucan as well as the flux recovery was markedly improved with no important reduction of the permeate flux. Finally, polysulfone membrane was applied in the pilot cross-flow module for the ultrafiltration of β-glucan containing feeds (<600
mg/L) recovered from the industrial oat mill waste. Results indicated that the optimized ultrafiltration process (polysulfone in cross-flow module, with transmembrane pressure ≤2
bar and β-glucan concentrations
<
600
mg/L) could be utilized in order to recover β-glucan from the oat mill waste feeds and clarify them from smaller organic and inorganic compounds. A disadvantage of the latter application was the small degree of separation between β-glucan and proteins.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.memsci.2011.02.032</doi><tpages>11</tpages></addata></record> |
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subjects | artificial membranes Beta glucan beta-glucans cellulose Chemistry Colloidal state and disperse state Dietary fiber Exact sciences and technology General and physical chemistry inorganic compounds Macromolecules Membranes molecular weight monitoring oats Operational features Polysaccharides proteins Ultrafiltration wastes |
title | Ultrafiltration optimization for the recovery of β-glucan from oat mill waste |
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