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Compatibility of column inlet and adsorbent designs for processing of corn endosperm extract by expanded bed adsorption

Corn has emerged as a viable host for expression of recombinant proteins; targeted expression to the endosperm has received particular attention. The protein extracts from corn endosperm differ from those of traditional hosts in regard to the nature of residual solids and extracted matrix contaminan...

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Published in:Biotechnology and bioengineering 2004-08, Vol.87 (3), p.324-336
Main Authors: Menkhaus, T.J, Glatz, C.E
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description Corn has emerged as a viable host for expression of recombinant proteins; targeted expression to the endosperm has received particular attention. The protein extracts from corn endosperm differ from those of traditional hosts in regard to the nature of residual solids and extracted matrix contaminants. Each of these differences presents reasons for considering expanded bed adsorption for product capture and new considerations for limitations of the method. In this work three inlet-flow distribution devices (mesh, glass ballotini, and localized mixing) and six adsorbents with different physical (size and density), chemical (ligand), and base matrix properties were evaluated to determine conditions compatible with processing of crude corn endosperm extract by expanded bed adsorption. Of the inlet devices evaluated, the design with localized mixing at the inlet (as produced commercially by UpFront Chromatography A/S, Copenhagen, DK) allowed solids up to 550 micrometer into the column without clogging for all flow rates evaluated. A mesh at the inlet with size restriction of either 50 micrometer or 80 micrometer became clogged with very small corn particles (< 44 micrometer). When glass ballotini was used, large particles (550 micrometer) passed through for high flow rates (570 cm/h), but even small (< 44 micrometer) particles became trapped at a lower flow rate (180 cm/h). The physical and chemical properties of the resin determined whether solids could be eluted. The denser UpFront adsorbents allowed for complete elution of larger and more concentrated corn solids than the currently available Amersham Streamline adsorbents (Amersham Biosciences, Piscataway, NJ) as a result of the former's higher flow rate for the desired 2x expansion (570 cm/h for UpFront vs. 180 cm/h for Streamline). All corn solids < 162 micrometer eluted through nonderivatized UpFront resin. Larger corn solids began to accumulate due to their elevated sedimentation velocities. Feeds of < 44 micrometer solids at 0.45% and 2.0% dry weight successfully eluted through ion exchange adsorbents (DEAE and SP) from UpFront. However, significant accumulation occurred when the solids size increased to a feed of < 96 micrometer solids, thus indicating a weak interaction between corn solids and both forms of ion exchange ligands. Expanded beds operated with Streamline ion exchange adsorbents (DEAE and SP) did not allow full elution of corn solids of < 44 micrometer. A hyperdiffuse style EBA resin prod
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The protein extracts from corn endosperm differ from those of traditional hosts in regard to the nature of residual solids and extracted matrix contaminants. Each of these differences presents reasons for considering expanded bed adsorption for product capture and new considerations for limitations of the method. In this work three inlet-flow distribution devices (mesh, glass ballotini, and localized mixing) and six adsorbents with different physical (size and density), chemical (ligand), and base matrix properties were evaluated to determine conditions compatible with processing of crude corn endosperm extract by expanded bed adsorption. Of the inlet devices evaluated, the design with localized mixing at the inlet (as produced commercially by UpFront Chromatography A/S, Copenhagen, DK) allowed solids up to 550 micrometer into the column without clogging for all flow rates evaluated. 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Bioeng</addtitle><description><![CDATA[Corn has emerged as a viable host for expression of recombinant proteins; targeted expression to the endosperm has received particular attention. The protein extracts from corn endosperm differ from those of traditional hosts in regard to the nature of residual solids and extracted matrix contaminants. Each of these differences presents reasons for considering expanded bed adsorption for product capture and new considerations for limitations of the method. In this work three inlet-flow distribution devices (mesh, glass ballotini, and localized mixing) and six adsorbents with different physical (size and density), chemical (ligand), and base matrix properties were evaluated to determine conditions compatible with processing of crude corn endosperm extract by expanded bed adsorption. 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In this work three inlet-flow distribution devices (mesh, glass ballotini, and localized mixing) and six adsorbents with different physical (size and density), chemical (ligand), and base matrix properties were evaluated to determine conditions compatible with processing of crude corn endosperm extract by expanded bed adsorption. Of the inlet devices evaluated, the design with localized mixing at the inlet (as produced commercially by UpFront Chromatography A/S, Copenhagen, DK) allowed solids up to 550 micrometer into the column without clogging for all flow rates evaluated. A mesh at the inlet with size restriction of either 50 micrometer or 80 micrometer became clogged with very small corn particles (< 44 micrometer). When glass ballotini was used, large particles (550 micrometer) passed through for high flow rates (570 cm/h), but even small (< 44 micrometer) particles became trapped at a lower flow rate (180 cm/h). The physical and chemical properties of the resin determined whether solids could be eluted. The denser UpFront adsorbents allowed for complete elution of larger and more concentrated corn solids than the currently available Amersham Streamline adsorbents (Amersham Biosciences, Piscataway, NJ) as a result of the former's higher flow rate for the desired 2x expansion (570 cm/h for UpFront vs. 180 cm/h for Streamline). All corn solids < 162 micrometer eluted through nonderivatized UpFront resin. Larger corn solids began to accumulate due to their elevated sedimentation velocities. Feeds of < 44 micrometer solids at 0.45% and 2.0% dry weight successfully eluted through ion exchange adsorbents (DEAE and SP) from UpFront. However, significant accumulation occurred when the solids size increased to a feed of < 96 micrometer solids, thus indicating a weak interaction between corn solids and both forms of ion exchange ligands. Expanded beds operated with Streamline ion exchange adsorbents (DEAE and SP) did not allow full elution of corn solids of < 44 micrometer. A hyperdiffuse style EBA resin produced by Biosepra (Ciphergen Biosystems, Fremont, CA) with CM functionality showed a severe interaction with corn solids that collapsed the expanded bed and could not be eliminated with elevated flow rates or higher salt concentration.]]></abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc., A Wiley Company</pub><pmid>15281107</pmid><doi>10.1002/bit.20117</doi><tpages>13</tpages><oa>free_for_read</oa></addata></record>
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subjects Adsorption
Biotechnology
Chromatography
Chromatography, Ion Exchange - instrumentation
Chromatography, Ion Exchange - methods
column design
Contaminants
Corn
corn endosperm
corn solid elution
EBA resin
Endosperm
Equipment Design
Equipment Failure Analysis
expanded bed adsorption (EBA)
Gene expression
Ion exchange
Ion Exchange Resins - chemistry
Particle Size
Plant Extracts - chemistry
Plant Extracts - isolation & purification
Plant Proteins - chemistry
Plant Proteins - genetics
Plant Proteins - isolation & purification
Protein Binding
protein purification
Proteins
Q1
Recombinant Proteins - chemistry
Recombinant Proteins - isolation & purification
Resins
Salts
Sedimentation
Seeds - embryology
Seeds - genetics
Seeds - metabolism
Styles
Substance P
Transgenic plants
Ultrafiltration - instrumentation
Ultrafiltration - methods
Velocity
Zea mays - embryology
Zea mays - genetics
Zea mays - metabolism
title Compatibility of column inlet and adsorbent designs for processing of corn endosperm extract by expanded bed adsorption
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