Characterization of PAD-fusion proteins and immobilized PAD on different carrier materials. (A) Denaturing 16% SDS-PAGE analysis of 4 μg of each PAD fusion protein after heterologous expression in E. coli and purification via a C-terminal 6×His-tag. The proteins were obtained in purities >95% according to grayscale analysis. Lane 1: PAD (20.4 kDa); Lane 2: PAD-ST (21.8 kDa); Lane 3: PAD-HOB (53.8 kDa); Marker: PageRuler prestained protein ladder (Thermo Scientific). Molecular weight of to the monomer is given. (B) Enzymatic activity in (μmol pCA μmol PAD −1 min −1 ) of the PAD variants by using 0.1 mM p-coumaric acid (pCA) as substrate, determined by an absorbance-based assay in PAD Buffer (25 mM potassium phosphate buffer, pH 6) at 30 °C. (C) Specific activities per milligram of carrier material of PAD-functionalized SCmagnetosomes (PAD-ST@Mag; yellow) in a batch reaction in comparison to the alternative magnetically immobilizable biocatalyst systems. The conversion of pCA to pHS through PAD-ST@Mag, PAD-ST immobilized on SC-Dynabeads (PAD-ST@Dyn; dark blue), or PAD-HOB immobilized on CH-Dynabeads (PAD-HOB@Dyn; light blue) was monitored at different points in time by using HPLC analysis. All experiments were performed in PAD-Buffer at 30 °C and 600 rpm at least in duplicates by using different batches of magnetosomes or particles.

Characterization of PAD-fusion proteins and immobilized PAD on different carrier materials. (A) Denaturing 16% SDS-PAGE analysis of 4 μg of each PAD fusion protein after heterologous expression in E. coli and purification via a C-terminal 6×His-tag. The proteins were obtained in purities >95% according to grayscale analysis. Lane 1: PAD (20.4 kDa); Lane 2: PAD-ST (21.8 kDa); Lane 3: PAD-HOB (53.8 kDa); Marker: PageRuler prestained protein ladder (Thermo Scientific). Molecular weight of to the monomer is given. (B) Enzymatic activity in (μmol pCA μmol PAD −1 min −1 ) of the PAD variants by using 0.1 mM p-coumaric acid (pCA) as substrate, determined by an absorbance-based assay in PAD Buffer (25 mM potassium phosphate buffer, pH 6) at 30 °C. (C) Specific activities per milligram of carrier material of PAD-functionalized SCmagnetosomes (PAD-ST@Mag; yellow) in a batch reaction in comparison to the alternative magnetically immobilizable biocatalyst systems. The conversion of pCA to pHS through PAD-ST@Mag, PAD-ST immobilized on SC-Dynabeads (PAD-ST@Dyn; dark blue), or PAD-HOB immobilized on CH-Dynabeads (PAD-HOB@Dyn; light blue) was monitored at different points in time by using HPLC analysis. All experiments were performed in PAD-Buffer at 30 °C and 600 rpm at least in duplicates by using different batches of magnetosomes or particles.

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Biocatalysis in flow reactor systems is of increasing importance for the transformation of the chemical industry. However, the necessary immobilization of biocatalysts remains a challenge. We here demonstrate that biogenic magnetic nanoparticles, so-called magnetosomes, represent an attractive alternative for the development of nanoscale particle f...

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... potentially detrimental influence of the binding tags on the biocatalyst's activity has to be investigated. However, we found that the fusion of PAD with the tags used in this work could be heterologously expressed in high purity ( Figure 5A) with no significant differences in the substrate conversion rate ( Figure 5B). Furthermore, maximizing the volumetric activity of flow reactors is a crucial parameter for their efficiency and strongly depends on the effective surface area and binding capacity of the support matrix used. ...
Context 2
... potentially detrimental influence of the binding tags on the biocatalyst's activity has to be investigated. However, we found that the fusion of PAD with the tags used in this work could be heterologously expressed in high purity ( Figure 5A) with no significant differences in the substrate conversion rate ( Figure 5B). Furthermore, maximizing the volumetric activity of flow reactors is a crucial parameter for their efficiency and strongly depends on the effective surface area and binding capacity of the support matrix used. ...
Context 3
... to application in a flow process, the PAD activity per milligram of carrier material was analyzed via the conversion of p-coumaric acid (pCA) to p-hydroxystyrene (pHS) in a batch assay. PAD-ST@Mag showed a superior activity per milligram of carrier material in comparison to PAD-ST@Dyn and PAD-HOB@Dyn ( Figure 5C), which might be due to the higher surface area of the magnetosome nano-biocatalyst in comparison to the Dynabeads. ...
Context 4
... slow decline in reactivity of the PAD-ST@Mag could potentially be due to disintegration of the magnetosomes. However, we could not detect obvious changes in magnetosome morphology when comparing particles before and after application in the flow reactor ( Figure S5). On the contrary, the stability of the PAD appears to be improved by immobilization. ...

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