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Microfluidic multi-input reactor for biocatalytic synthesis using transketolase()

Biocatalytic synthesis in continuous-flow microreactors is of increasing interest for the production of specialty chemicals. However, the yield of production achievable in these reactors can be limited by the adverse effects of high substrate concentration on the biocatalyst, including inhibition an...

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Detalles Bibliográficos
Autores principales: Lawrence, James, O'Sullivan, Brian, Lye, Gary J., Wohlgemuth, Roland, Szita, Nicolas
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Elsevier Science 2013
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3724052/
https://www.ncbi.nlm.nih.gov/pubmed/24187515
http://dx.doi.org/10.1016/j.molcatb.2013.05.016
Descripción
Sumario:Biocatalytic synthesis in continuous-flow microreactors is of increasing interest for the production of specialty chemicals. However, the yield of production achievable in these reactors can be limited by the adverse effects of high substrate concentration on the biocatalyst, including inhibition and denaturation. Fed-batch reactors have been developed in order to overcome this problem, but no continuous-flow solution exists. We present the design of a novel multi-input microfluidic reactor, capable of substrate feeding at multiple points, as a first step towards overcoming these problems in a continuous-flow setting. Using the transketolase-(TK) catalysed reaction of lithium hydroxypyruvate (HPA) and glycolaldehyde (GA) to l-erythrulose (ERY), we demonstrate the transposition of a fed-batch substrate feeding strategy to our microfluidic reactor. We obtained a 4.5-fold increase in output concentration and a 5-fold increase in throughput compared with a single input reactor.