Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane

Membrane chromatography can overcome some of the limitations of packed bed column chromatography but preparation of adsorptive membranes usually involves complex and harsh chemical modifications. Mixed matrix membranes (MMMs) require only the physical incorporation of an ion exchange resin into the...

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Main Authors: Syed Mohd Saufi, Tuan Chik, J. Fee, Conan
Format: Article
Language:English
Published: Elsevier B.V. 2011
Subjects:
Online Access:http://umpir.ump.edu.my/id/eprint/25437/1/Simultaneous%20anion%20and%20cation%20exchange%20chromatography%20of%20whey%20proteins.pdf
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author Syed Mohd Saufi, Tuan Chik
J. Fee, Conan
author_facet Syed Mohd Saufi, Tuan Chik
J. Fee, Conan
author_sort Syed Mohd Saufi, Tuan Chik
collection UMP
description Membrane chromatography can overcome some of the limitations of packed bed column chromatography but preparation of adsorptive membranes usually involves complex and harsh chemical modifications. Mixed matrix membranes (MMMs) require only the physical incorporation of an ion exchange resin into the membrane polymer solution prior to membrane casting. An advantage of MMMs not previously exploited is that resins with differing adsorptive functionalities can be conveniently embedded within a single membrane at any desired ratio. This presents the opportunity to customize an adsorptive membrane to suit the expected protein profile of a raw feed stream e.g. bovine whey or serum. In this work, a novel mixed mode interaction MMM customized to extract all major proteins from bovine whey was synthesized in a single membrane by incorporating 42.5 wt% Lewatit MP500 anionic resin and 7.5 wt% SP Sepharose cationic resin into an ethylene vinyl alcohol base polymer casting solution. The mixed mode MMM developed was able to bind both basic and acidic proteins simultaneously from whey, with binding capacities of 7.16 ± 2.24 mg α-lactalbumin g−1 membrane, 11.40 ± 0.73 mg lactoferrin (LF) g−1 membrane, 59.21 ± 9.90 mg β-lactoglobulin g−1 membrane and 6.79 ± 1.11 mg immunoglobulin G g−1 membrane (85 mg total protein g−1 membrane) during batch fractionation of LF-spiked whey. A 1000 m2 spiral-wound membrane module (200 L membrane volume, 1 m3 module volume) is predicted to be able to produce approximately 25 kg total whey protein per h.
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spelling UMPir254372019-12-24T02:34:19Z http://umpir.ump.edu.my/id/eprint/25437/ Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane Syed Mohd Saufi, Tuan Chik J. Fee, Conan TP Chemical technology Membrane chromatography can overcome some of the limitations of packed bed column chromatography but preparation of adsorptive membranes usually involves complex and harsh chemical modifications. Mixed matrix membranes (MMMs) require only the physical incorporation of an ion exchange resin into the membrane polymer solution prior to membrane casting. An advantage of MMMs not previously exploited is that resins with differing adsorptive functionalities can be conveniently embedded within a single membrane at any desired ratio. This presents the opportunity to customize an adsorptive membrane to suit the expected protein profile of a raw feed stream e.g. bovine whey or serum. In this work, a novel mixed mode interaction MMM customized to extract all major proteins from bovine whey was synthesized in a single membrane by incorporating 42.5 wt% Lewatit MP500 anionic resin and 7.5 wt% SP Sepharose cationic resin into an ethylene vinyl alcohol base polymer casting solution. The mixed mode MMM developed was able to bind both basic and acidic proteins simultaneously from whey, with binding capacities of 7.16 ± 2.24 mg α-lactalbumin g−1 membrane, 11.40 ± 0.73 mg lactoferrin (LF) g−1 membrane, 59.21 ± 9.90 mg β-lactoglobulin g−1 membrane and 6.79 ± 1.11 mg immunoglobulin G g−1 membrane (85 mg total protein g−1 membrane) during batch fractionation of LF-spiked whey. A 1000 m2 spiral-wound membrane module (200 L membrane volume, 1 m3 module volume) is predicted to be able to produce approximately 25 kg total whey protein per h. Elsevier B.V. 2011 Article PeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/25437/1/Simultaneous%20anion%20and%20cation%20exchange%20chromatography%20of%20whey%20proteins.pdf Syed Mohd Saufi, Tuan Chik and J. Fee, Conan (2011) Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane. Journal of Chromatography A, 1218 (50). pp. 9003-9009. ISSN 0021-9673. (Published) https://doi.org/10.1016/j.chroma.2011.09.045 https://doi.org/10.1016/j.chroma.2011.09.045
spellingShingle TP Chemical technology
Syed Mohd Saufi, Tuan Chik
J. Fee, Conan
Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane
title Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane
title_full Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane
title_fullStr Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane
title_full_unstemmed Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane
title_short Simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane
title_sort simultaneous anion and cation exchange chromatography of whey proteins using a customizable mixed matrix membrane
topic TP Chemical technology
url http://umpir.ump.edu.my/id/eprint/25437/1/Simultaneous%20anion%20and%20cation%20exchange%20chromatography%20of%20whey%20proteins.pdf
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