Site-specific protein modification using immobilized sortase in batch and continuous-flow systems
Sortase A can be used for the site-specific modification of proteins. This protocol describes its immobilization on Sepharose beads, allowing for larger-scale continuous flow reactions or easy separation from the enzyme in batch reactions. Transpeptidation catalyzed by sortase A allows the preparati...
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Published in | Nature protocols Vol. 10; no. 3; pp. 508 - 516 |
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Main Authors | , , , , , , , , , |
Format | Journal Article |
Language | English |
Published |
London
Nature Publishing Group UK
01.03.2015
Nature Publishing Group |
Subjects | |
Online Access | Get full text |
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Summary: | Sortase A can be used for the site-specific modification of proteins. This protocol describes its immobilization on Sepharose beads, allowing for larger-scale continuous flow reactions or easy separation from the enzyme in batch reactions.
Transpeptidation catalyzed by sortase A allows the preparation of proteins that are site-specifically and homogeneously modified with a wide variety of functional groups, such as fluorophores, PEG moieties, lipids, glycans, bio-orthogonal reactive groups and affinity handles. This protocol describes immobilization of sortase A on a solid support (Sepharose beads). Immobilization of sortase A simplifies downstream purification of a protein of interest after labeling of its N or C terminus. Smaller batch and larger-scale continuous-flow reactions require only a limited amount of enzyme. The immobilized enzyme can be reused for multiple cycles of protein modification reactions. The described protocol also works with a Ca
2+
-independent variant of sortase A with increased catalytic activity. This heptamutant variant of sortase A (7M) was generated by combining previously published mutations, and this immobilized enzyme can be used for the modification of calcium-senstive substrates or in instances in which low temperatures are needed. Preparation of immobilized sortase A takes 1–2 d. Batch reactions take 3–12 h and flow reactions proceed at 0.5 ml h
−1
, depending on the geometry of the reactor used. |
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Bibliography: | ObjectType-Article-1 SourceType-Scholarly Journals-1 ObjectType-Feature-2 content type line 23 Current address: Bio-Organic Chemistry, Stratingh Institute for Chemistry, University of Groningen, Groningen, The Netherlands These authors contributed equally |
ISSN: | 1754-2189 1750-2799 |
DOI: | 10.1038/nprot.2015.026 |