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Partition of tannery wastewater proteins in aqueous two-phase poly (ethylene glycol)-magnesium sulfate systems: Effects of molecular weights and pH
The partitioning behavior of soluble proteins from tannery wastewater using aqueous two-phase system (ATPS) was investigated. An ATPS polyethylene glycol ( PEG ) / MgSO 4 was examined with regard to the effects of PEG molecular weight (MW) and concentration, MgSO 4 concentration, pH and NaCl concent...
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Published in: | Chemical engineering science 2007-02, Vol.62 (4), p.969-978 |
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container_title | Chemical engineering science |
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creator | Saravanan, S. Rao, J. Raghava Murugesan, T. Nair, Balachandran Unni Ramasami, T. |
description | The partitioning behavior of soluble proteins from tannery wastewater using aqueous two-phase system (ATPS) was investigated. An ATPS polyethylene glycol
(
PEG
)
/
MgSO
4
was examined with regard to the effects of PEG molecular weight (MW) and concentration,
MgSO
4
concentration, pH and NaCl concentration on protein partition and extraction. The partition coefficients measured for soluble proteins were proportional to the difference in PEG concentration between the phases. The MW and concentration of PEG were found to have significant effects on protein partition and extraction with low MW PEG4000 showing the best conditions for the partitioning of protein in
PEG
+
MgSO
4
+
water
system. Sulfate salt was chosen as the phase-forming salt because of its ability to promote hydrophobic difference between the phases. This system was operated at room temperature
(
30
∘
C
)
. Increase in pH of the system increases the partition coefficient of proteins from tannery wastewater. The addition of sodium chloride showed significant influence on the partition coefficient. ATPS comprising PEG4000-magnesium sulfate provided a means for the recovery of proteins from tannery wastewater. The maximum percentage yield of protein extracted is 82.68%. |
doi_str_mv | 10.1016/j.ces.2006.10.025 |
format | article |
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(
PEG
)
/
MgSO
4
was examined with regard to the effects of PEG molecular weight (MW) and concentration,
MgSO
4
concentration, pH and NaCl concentration on protein partition and extraction. The partition coefficients measured for soluble proteins were proportional to the difference in PEG concentration between the phases. The MW and concentration of PEG were found to have significant effects on protein partition and extraction with low MW PEG4000 showing the best conditions for the partitioning of protein in
PEG
+
MgSO
4
+
water
system. Sulfate salt was chosen as the phase-forming salt because of its ability to promote hydrophobic difference between the phases. This system was operated at room temperature
(
30
∘
C
)
. Increase in pH of the system increases the partition coefficient of proteins from tannery wastewater. The addition of sodium chloride showed significant influence on the partition coefficient. ATPS comprising PEG4000-magnesium sulfate provided a means for the recovery of proteins from tannery wastewater. The maximum percentage yield of protein extracted is 82.68%.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/j.ces.2006.10.025</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Aqueous two-phase systems ; Bovine serum albumin ; Chemical engineering ; Exact sciences and technology ; General purification processes ; Globular proteins ; Magnesium sulfate ; Partition coefficient ; Pollution ; Polyethylene glycol ; Wastewaters ; Water treatment and pollution</subject><ispartof>Chemical engineering science, 2007-02, Vol.62 (4), p.969-978</ispartof><rights>2006 Elsevier Ltd</rights><rights>2007 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c389t-b34730184f9dc0ab3136ac09a73edbcf74330e51e60f5279822bfa7b35b20ba23</citedby><cites>FETCH-LOGICAL-c389t-b34730184f9dc0ab3136ac09a73edbcf74330e51e60f5279822bfa7b35b20ba23</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=18429683$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Saravanan, S.</creatorcontrib><creatorcontrib>Rao, J. Raghava</creatorcontrib><creatorcontrib>Murugesan, T.</creatorcontrib><creatorcontrib>Nair, Balachandran Unni</creatorcontrib><creatorcontrib>Ramasami, T.</creatorcontrib><title>Partition of tannery wastewater proteins in aqueous two-phase poly (ethylene glycol)-magnesium sulfate systems: Effects of molecular weights and pH</title><title>Chemical engineering science</title><description>The partitioning behavior of soluble proteins from tannery wastewater using aqueous two-phase system (ATPS) was investigated. An ATPS polyethylene glycol
(
PEG
)
/
MgSO
4
was examined with regard to the effects of PEG molecular weight (MW) and concentration,
MgSO
4
concentration, pH and NaCl concentration on protein partition and extraction. The partition coefficients measured for soluble proteins were proportional to the difference in PEG concentration between the phases. The MW and concentration of PEG were found to have significant effects on protein partition and extraction with low MW PEG4000 showing the best conditions for the partitioning of protein in
PEG
+
MgSO
4
+
water
system. Sulfate salt was chosen as the phase-forming salt because of its ability to promote hydrophobic difference between the phases. This system was operated at room temperature
(
30
∘
C
)
. Increase in pH of the system increases the partition coefficient of proteins from tannery wastewater. The addition of sodium chloride showed significant influence on the partition coefficient. ATPS comprising PEG4000-magnesium sulfate provided a means for the recovery of proteins from tannery wastewater. The maximum percentage yield of protein extracted is 82.68%.</description><subject>Applied sciences</subject><subject>Aqueous two-phase systems</subject><subject>Bovine serum albumin</subject><subject>Chemical engineering</subject><subject>Exact sciences and technology</subject><subject>General purification processes</subject><subject>Globular proteins</subject><subject>Magnesium sulfate</subject><subject>Partition coefficient</subject><subject>Pollution</subject><subject>Polyethylene glycol</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNqFUcuO1DAQjBBIDAsfwM0XEBwy-JEnnNBqH0grwQHOluO0Zzxy7OB2GOU7-GEczUrc4NTqVnWVqqooXjO6Z5Q1H057DbjnlDZ531NePyl2rGtFWVW0flrsKKV9yWvaPy9eIJ7y2raM7orf31RMNtngSTAkKe8hruSsMMFZJYhkjiGB9UisJ-rnAmFBks6hnI8KgczBreQdpOPqwAM5uFUH976c1MED2mUiuDiTeQiumXHCj-TGGNAJN7UpONCLU5GcwR6O-aj8SOb7l8UzoxzCq8d5Vfy4vfl-fV8-fL37cv35odSi61M5iKoVlHWV6UdN1SCYaJSmvWoFjIM2bSUEhZpBQ03N277jfDCqHUQ9cDooLq6Ktxfe7DE7wyQnixqcU36zKXlf142g_weyPmsxWmcguwB1DIgRjJyjnVRcJaNy60meZO5Jbj1tp9xT_nnzSK5QK2ei8tri38eu4n3TiYz7dMFBjuSXhShRW_AaRhtzonIM9h8qfwDcEasI</recordid><startdate>20070201</startdate><enddate>20070201</enddate><creator>Saravanan, S.</creator><creator>Rao, J. Raghava</creator><creator>Murugesan, T.</creator><creator>Nair, Balachandran Unni</creator><creator>Ramasami, T.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7U5</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>L7M</scope></search><sort><creationdate>20070201</creationdate><title>Partition of tannery wastewater proteins in aqueous two-phase poly (ethylene glycol)-magnesium sulfate systems: Effects of molecular weights and pH</title><author>Saravanan, S. ; Rao, J. Raghava ; Murugesan, T. ; Nair, Balachandran Unni ; Ramasami, T.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c389t-b34730184f9dc0ab3136ac09a73edbcf74330e51e60f5279822bfa7b35b20ba23</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Applied sciences</topic><topic>Aqueous two-phase systems</topic><topic>Bovine serum albumin</topic><topic>Chemical engineering</topic><topic>Exact sciences and technology</topic><topic>General purification processes</topic><topic>Globular proteins</topic><topic>Magnesium sulfate</topic><topic>Partition coefficient</topic><topic>Pollution</topic><topic>Polyethylene glycol</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Saravanan, S.</creatorcontrib><creatorcontrib>Rao, J. Raghava</creatorcontrib><creatorcontrib>Murugesan, T.</creatorcontrib><creatorcontrib>Nair, Balachandran Unni</creatorcontrib><creatorcontrib>Ramasami, T.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Saravanan, S.</au><au>Rao, J. Raghava</au><au>Murugesan, T.</au><au>Nair, Balachandran Unni</au><au>Ramasami, T.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Partition of tannery wastewater proteins in aqueous two-phase poly (ethylene glycol)-magnesium sulfate systems: Effects of molecular weights and pH</atitle><jtitle>Chemical engineering science</jtitle><date>2007-02-01</date><risdate>2007</risdate><volume>62</volume><issue>4</issue><spage>969</spage><epage>978</epage><pages>969-978</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>The partitioning behavior of soluble proteins from tannery wastewater using aqueous two-phase system (ATPS) was investigated. An ATPS polyethylene glycol
(
PEG
)
/
MgSO
4
was examined with regard to the effects of PEG molecular weight (MW) and concentration,
MgSO
4
concentration, pH and NaCl concentration on protein partition and extraction. The partition coefficients measured for soluble proteins were proportional to the difference in PEG concentration between the phases. The MW and concentration of PEG were found to have significant effects on protein partition and extraction with low MW PEG4000 showing the best conditions for the partitioning of protein in
PEG
+
MgSO
4
+
water
system. Sulfate salt was chosen as the phase-forming salt because of its ability to promote hydrophobic difference between the phases. This system was operated at room temperature
(
30
∘
C
)
. Increase in pH of the system increases the partition coefficient of proteins from tannery wastewater. The addition of sodium chloride showed significant influence on the partition coefficient. ATPS comprising PEG4000-magnesium sulfate provided a means for the recovery of proteins from tannery wastewater. The maximum percentage yield of protein extracted is 82.68%.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ces.2006.10.025</doi><tpages>10</tpages></addata></record> |
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language | eng |
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source | ScienceDirect Freedom Collection 2022-2024 |
subjects | Applied sciences Aqueous two-phase systems Bovine serum albumin Chemical engineering Exact sciences and technology General purification processes Globular proteins Magnesium sulfate Partition coefficient Pollution Polyethylene glycol Wastewaters Water treatment and pollution |
title | Partition of tannery wastewater proteins in aqueous two-phase poly (ethylene glycol)-magnesium sulfate systems: Effects of molecular weights and pH |
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