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Evaluation of a novel methacrylate-based protein a resin for the purification of immunoglobulins and Fc-fusion proteins
Protein A affinity chromatography is a central part of most commercial monoclonal antibody and Fc‐fusion protein purification processes. In the last couple years an increasing number of new Protein A technologies have emerged. One of these new Protein A technologies consists of a novel, alkaline‐tol...
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Published in: | Biotechnology progress 2014-09, Vol.30 (5), p.1125-1136 |
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description | Protein A affinity chromatography is a central part of most commercial monoclonal antibody and Fc‐fusion protein purification processes. In the last couple years an increasing number of new Protein A technologies have emerged. One of these new Protein A technologies consists of a novel, alkaline‐tolerant, Protein A ligand coupled to a macroporous polymethacrylate base matrix that has been optimized for immunoglobulin (Ig) G capture. The resin is interesting from a technology perspective because the particle size and pore distribution of the base beads are reported to have been optimized for high IgG binding and fast mass transfer, while the Protein A ligand has been engineered for enhanced alkaline tolerance. This resin was subjected to a number of technical studies including evaluating dynamic and static binding capacities, alkaline stability, Protein A leachate propensity, impurity clearance, and pressure–flow behavior. The results demonstrated similar static binding capacities as those achieved with industry standard agarose Protein A resins, but marginally lower dynamic binding capacities. Removal of impurities from the process stream, particularly host cell proteins, was molecule dependent, but in most instances matched the performance of the agarose resins. This resin was stable in 0.1 M NaOH for at least 100 h with little loss in binding capacity, with Protein A ligand leakage levels comparable to values for the agarose resins. Pressure–flow experiments in lab‐scale chromatography columns demonstrated minimal resin compression at typical manufacturing flow rates. Prediction of resin compression in manufacturing scale columns did not suggest any pressure limitations upon scale up. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1125–1136, 2014 |
doi_str_mv | 10.1002/btpr.1951 |
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In the last couple years an increasing number of new Protein A technologies have emerged. One of these new Protein A technologies consists of a novel, alkaline‐tolerant, Protein A ligand coupled to a macroporous polymethacrylate base matrix that has been optimized for immunoglobulin (Ig) G capture. The resin is interesting from a technology perspective because the particle size and pore distribution of the base beads are reported to have been optimized for high IgG binding and fast mass transfer, while the Protein A ligand has been engineered for enhanced alkaline tolerance. This resin was subjected to a number of technical studies including evaluating dynamic and static binding capacities, alkaline stability, Protein A leachate propensity, impurity clearance, and pressure–flow behavior. The results demonstrated similar static binding capacities as those achieved with industry standard agarose Protein A resins, but marginally lower dynamic binding capacities. Removal of impurities from the process stream, particularly host cell proteins, was molecule dependent, but in most instances matched the performance of the agarose resins. This resin was stable in 0.1 M NaOH for at least 100 h with little loss in binding capacity, with Protein A ligand leakage levels comparable to values for the agarose resins. Pressure–flow experiments in lab‐scale chromatography columns demonstrated minimal resin compression at typical manufacturing flow rates. Prediction of resin compression in manufacturing scale columns did not suggest any pressure limitations upon scale up. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1125–1136, 2014</description><identifier>ISSN: 8756-7938</identifier><identifier>EISSN: 1520-6033</identifier><identifier>DOI: 10.1002/btpr.1951</identifier><identifier>PMID: 25045034</identifier><language>eng</language><publisher>United States: Blackwell Publishing Ltd</publisher><subject>alkaline stability ; binding capacities ; Bioseparations and Downstream Processing ; Chromatography, Affinity - methods ; Fc-fusion proteins ; Hydrogen-Ion Concentration ; Immunoglobulin Fc Fragments - chemistry ; Immunoglobulin Fc Fragments - isolation & purification ; Immunoglobulin Fc Fragments - metabolism ; Immunoglobulins - chemistry ; Immunoglobulins - isolation & purification ; Immunoglobulins - metabolism ; mAbs ; Methacrylates - chemistry ; Pressure ; pressure-flow profiles ; Protein A chromatography ; Protein Binding ; Protein Stability ; Recombinant Fusion Proteins - chemistry ; Recombinant Fusion Proteins - isolation & purification ; Recombinant Fusion Proteins - metabolism ; Staphylococcal Protein A - chemistry ; Staphylococcal Protein A - metabolism</subject><ispartof>Biotechnology progress, 2014-09, Vol.30 (5), p.1125-1136</ispartof><rights>2014 American Institute of Chemical Engineers</rights><rights>2014 American Institute of Chemical Engineers.</rights><rights>2014 American Institute of Chemical Engineers 2014</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c6211-3175327122bd9a4c7ecf82b82ece689d269439ba560a8455d08bc2c5c85812f43</citedby><cites>FETCH-LOGICAL-c6211-3175327122bd9a4c7ecf82b82ece689d269439ba560a8455d08bc2c5c85812f43</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>230,314,780,784,885,27924,27925</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/25045034$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>McCaw, Tyler R.</creatorcontrib><creatorcontrib>Koepf, Edward K.</creatorcontrib><creatorcontrib>Conley, Lynn</creatorcontrib><title>Evaluation of a novel methacrylate-based protein a resin for the purification of immunoglobulins and Fc-fusion proteins</title><title>Biotechnology progress</title><addtitle>Biotechnol Progress</addtitle><description>Protein A affinity chromatography is a central part of most commercial monoclonal antibody and Fc‐fusion protein purification processes. In the last couple years an increasing number of new Protein A technologies have emerged. One of these new Protein A technologies consists of a novel, alkaline‐tolerant, Protein A ligand coupled to a macroporous polymethacrylate base matrix that has been optimized for immunoglobulin (Ig) G capture. The resin is interesting from a technology perspective because the particle size and pore distribution of the base beads are reported to have been optimized for high IgG binding and fast mass transfer, while the Protein A ligand has been engineered for enhanced alkaline tolerance. This resin was subjected to a number of technical studies including evaluating dynamic and static binding capacities, alkaline stability, Protein A leachate propensity, impurity clearance, and pressure–flow behavior. The results demonstrated similar static binding capacities as those achieved with industry standard agarose Protein A resins, but marginally lower dynamic binding capacities. Removal of impurities from the process stream, particularly host cell proteins, was molecule dependent, but in most instances matched the performance of the agarose resins. This resin was stable in 0.1 M NaOH for at least 100 h with little loss in binding capacity, with Protein A ligand leakage levels comparable to values for the agarose resins. Pressure–flow experiments in lab‐scale chromatography columns demonstrated minimal resin compression at typical manufacturing flow rates. Prediction of resin compression in manufacturing scale columns did not suggest any pressure limitations upon scale up. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1125–1136, 2014</description><subject>alkaline stability</subject><subject>binding capacities</subject><subject>Bioseparations and Downstream Processing</subject><subject>Chromatography, Affinity - methods</subject><subject>Fc-fusion proteins</subject><subject>Hydrogen-Ion Concentration</subject><subject>Immunoglobulin Fc Fragments - chemistry</subject><subject>Immunoglobulin Fc Fragments - isolation & purification</subject><subject>Immunoglobulin Fc Fragments - metabolism</subject><subject>Immunoglobulins - chemistry</subject><subject>Immunoglobulins - isolation & purification</subject><subject>Immunoglobulins - metabolism</subject><subject>mAbs</subject><subject>Methacrylates - chemistry</subject><subject>Pressure</subject><subject>pressure-flow profiles</subject><subject>Protein A chromatography</subject><subject>Protein Binding</subject><subject>Protein Stability</subject><subject>Recombinant Fusion Proteins - chemistry</subject><subject>Recombinant Fusion Proteins - isolation & purification</subject><subject>Recombinant Fusion Proteins - metabolism</subject><subject>Staphylococcal Protein A - chemistry</subject><subject>Staphylococcal Protein A - metabolism</subject><issn>8756-7938</issn><issn>1520-6033</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2014</creationdate><recordtype>article</recordtype><sourceid>24P</sourceid><recordid>eNqN0U9v0zAYBnALgVgpHPgCKBIXOGTz_zgXJCjbQJoGQgWOluO8WT0cu9hJR789qVoqQELi5IN_7yP7fRB6SvApwZieNcM6nZJakHtoRgTFpcSM3UczVQlZVjVTJ-hRzrcYY4UlfYhOqMBcYMZn6O58Y_xoBhdDEbvCFCFuwBc9DCtj09abAcrGZGiLdYoDuDCRBHk6u5iKYQXFekyuc_YY4fp-DPHGx2b0LuTChLa4sGU35h04pOTH6EFnfIYnh3OOPl-cLxfvyqsPl-8Xr69KKykhJSOVYLQilDZtbbitwHaKNoqCBanqlsqas7oxQmKjuBAtVo2lVlglFKEdZ3P0ap-7HpseWgthSMbrdXK9SVsdjdN_3gS30jdxozknQky7m6MXh4AUv4-QB927bMF7EyCOWRMpOakpZ_g_KK4FlgTLiT7_i97GMYVpE5MSihJeUzWpl3tlU8w5QXd8N8F617zeNa93zU_22e8fPcpfVU_gbA_unIftv5P0m-XHT4fIcj_h8gA_jhMmfdOyYpXQX68v9WJZLb68JddasJ_gRskD</recordid><startdate>201409</startdate><enddate>201409</enddate><creator>McCaw, Tyler R.</creator><creator>Koepf, Edward K.</creator><creator>Conley, Lynn</creator><general>Blackwell Publishing Ltd</general><general>Wiley Subscription Services, Inc</general><general>BlackWell Publishing Ltd</general><scope>BSCLL</scope><scope>24P</scope><scope>WIN</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QL</scope><scope>7QO</scope><scope>7T7</scope><scope>7U7</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>M7N</scope><scope>P64</scope><scope>7X8</scope><scope>7QH</scope><scope>7T5</scope><scope>7UA</scope><scope>F1W</scope><scope>H94</scope><scope>H96</scope><scope>L.G</scope><scope>5PM</scope></search><sort><creationdate>201409</creationdate><title>Evaluation of a novel methacrylate-based protein a resin for the purification of immunoglobulins and Fc-fusion proteins</title><author>McCaw, Tyler R. ; Koepf, Edward K. ; Conley, Lynn</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c6211-3175327122bd9a4c7ecf82b82ece689d269439ba560a8455d08bc2c5c85812f43</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2014</creationdate><topic>alkaline stability</topic><topic>binding capacities</topic><topic>Bioseparations and Downstream Processing</topic><topic>Chromatography, Affinity - methods</topic><topic>Fc-fusion proteins</topic><topic>Hydrogen-Ion Concentration</topic><topic>Immunoglobulin Fc Fragments - chemistry</topic><topic>Immunoglobulin Fc Fragments - isolation & purification</topic><topic>Immunoglobulin Fc Fragments - metabolism</topic><topic>Immunoglobulins - chemistry</topic><topic>Immunoglobulins - isolation & purification</topic><topic>Immunoglobulins - metabolism</topic><topic>mAbs</topic><topic>Methacrylates - chemistry</topic><topic>Pressure</topic><topic>pressure-flow profiles</topic><topic>Protein A chromatography</topic><topic>Protein Binding</topic><topic>Protein Stability</topic><topic>Recombinant Fusion Proteins - chemistry</topic><topic>Recombinant Fusion Proteins - isolation & purification</topic><topic>Recombinant Fusion Proteins - metabolism</topic><topic>Staphylococcal Protein A - chemistry</topic><topic>Staphylococcal Protein A - metabolism</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>McCaw, Tyler R.</creatorcontrib><creatorcontrib>Koepf, Edward K.</creatorcontrib><creatorcontrib>Conley, Lynn</creatorcontrib><collection>Istex</collection><collection>Wiley Open Access</collection><collection>Wiley Open Access</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Bacteriology Abstracts (Microbiology B)</collection><collection>Biotechnology Research Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Toxicology Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Algology Mycology and Protozoology Abstracts (Microbiology C)</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>MEDLINE - Academic</collection><collection>Aqualine</collection><collection>Immunology Abstracts</collection><collection>Water Resources Abstracts</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>AIDS and Cancer Research Abstracts</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy & Non-Living Resources</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>PubMed Central (Full Participant titles)</collection><jtitle>Biotechnology progress</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>McCaw, Tyler R.</au><au>Koepf, Edward K.</au><au>Conley, Lynn</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Evaluation of a novel methacrylate-based protein a resin for the purification of immunoglobulins and Fc-fusion proteins</atitle><jtitle>Biotechnology progress</jtitle><addtitle>Biotechnol Progress</addtitle><date>2014-09</date><risdate>2014</risdate><volume>30</volume><issue>5</issue><spage>1125</spage><epage>1136</epage><pages>1125-1136</pages><issn>8756-7938</issn><eissn>1520-6033</eissn><abstract>Protein A affinity chromatography is a central part of most commercial monoclonal antibody and Fc‐fusion protein purification processes. In the last couple years an increasing number of new Protein A technologies have emerged. One of these new Protein A technologies consists of a novel, alkaline‐tolerant, Protein A ligand coupled to a macroporous polymethacrylate base matrix that has been optimized for immunoglobulin (Ig) G capture. The resin is interesting from a technology perspective because the particle size and pore distribution of the base beads are reported to have been optimized for high IgG binding and fast mass transfer, while the Protein A ligand has been engineered for enhanced alkaline tolerance. This resin was subjected to a number of technical studies including evaluating dynamic and static binding capacities, alkaline stability, Protein A leachate propensity, impurity clearance, and pressure–flow behavior. The results demonstrated similar static binding capacities as those achieved with industry standard agarose Protein A resins, but marginally lower dynamic binding capacities. Removal of impurities from the process stream, particularly host cell proteins, was molecule dependent, but in most instances matched the performance of the agarose resins. This resin was stable in 0.1 M NaOH for at least 100 h with little loss in binding capacity, with Protein A ligand leakage levels comparable to values for the agarose resins. Pressure–flow experiments in lab‐scale chromatography columns demonstrated minimal resin compression at typical manufacturing flow rates. Prediction of resin compression in manufacturing scale columns did not suggest any pressure limitations upon scale up. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1125–1136, 2014</abstract><cop>United States</cop><pub>Blackwell Publishing Ltd</pub><pmid>25045034</pmid><doi>10.1002/btpr.1951</doi><tpages>12</tpages><oa>free_for_read</oa></addata></record> |
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subjects | alkaline stability binding capacities Bioseparations and Downstream Processing Chromatography, Affinity - methods Fc-fusion proteins Hydrogen-Ion Concentration Immunoglobulin Fc Fragments - chemistry Immunoglobulin Fc Fragments - isolation & purification Immunoglobulin Fc Fragments - metabolism Immunoglobulins - chemistry Immunoglobulins - isolation & purification Immunoglobulins - metabolism mAbs Methacrylates - chemistry Pressure pressure-flow profiles Protein A chromatography Protein Binding Protein Stability Recombinant Fusion Proteins - chemistry Recombinant Fusion Proteins - isolation & purification Recombinant Fusion Proteins - metabolism Staphylococcal Protein A - chemistry Staphylococcal Protein A - metabolism |
title | Evaluation of a novel methacrylate-based protein a resin for the purification of immunoglobulins and Fc-fusion proteins |
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