Abstract
Product removal from the continuous flow cell-free (CFCF) reactor still only partially solves some of the problems of this system, since the use of ultrafiltration membranes has some remaining limitations. These can be overcome by introducing an affinity system. A cell-free protein synthesis system has therefore been employed to produce bovine heart fatty acid binding protein (FABP) and bacterial chloramphenicol acetyltransferase (CAT) with and without fusion of the Strep-tag affinity peptide. These two fusion proteins were purified via a streptavidin and StrepTactin sepharose matrix respectively. No significant influence of the Strep-tag and the conditions during the affinity chromatogramphy on maturation or activity of the proteins were observed. In addition, quantitative removal of the fusion proteins during cell-free synthesis from a batch reaction and a semicontinuous flow cell-free (SFCF) reactor was achieved. The results document that it is possible to avoid the limitations of the ultrafiltration membranes during product removal from a CFCF reactor. The data presented show that the affinity system is also well suited for the development of a novel protein bioreactor.
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Lamla, T., Erdmann, V.A. (2002). Improved Batch Translation System Based on E. coli Extract. In: Spirin, A.S. (eds) Cell-Free Translation Systems. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-642-59379-6_2
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DOI: https://doi.org/10.1007/978-3-642-59379-6_2
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