Abstract
The first continuous production system of laminaribiose from sucrose and glucose in a bienzymatic reaction is reported in this study. Immobilized laminaribiose phosphorylase and sucrose phosphorylase were used in a packed bed reactor system comprising of a 3-cm glass column at 35 °C with a steady feeding flow rate of 0.1 ml/min. Factors affecting product formation including enzyme ratio, peal concept (both enzymes in one pearl or in separate pearls), and pearl size were studied. An enzyme ratio of 2:1 of laminaribiose phosphorylase (LP) to sucrose phosphorylase (SP) when encapsulated separately in bigger size peals resulted in higher concentration of product. Laminaribiose (0.4 g/(L h)) is produced in the optimized system at steady state. The reaction system proved to be operationally stable throughout 10 days of continuous processing. A half-life time of more than 9 days was observed for both biocatalysts.
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Abbreviations
- BR:
-
Batch reactor
- CR:
-
Continuous reactor
- GI:
-
Glucose isomerase
- Glc:
-
Glucose
- Fru:
-
Fructose
- G-1-P:
-
Glucose-1-phosphate
- HPAEC:
-
High-performance anion exchange chromatography
- ISPR:
-
In situ product removal
- Lam:
-
Laminaribiose
- Lam3:
-
Laminaritriose
- LP:
-
Laminaribiose phosphorylase
- PBR:
-
Packed bed reactor
- SP:
-
Sucrose phosphorylase
- Suc:
-
Sucrose
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Acknowledgements
This research was funded by the German Research Foundation (DFG) under grant numbers JO 355/3-2 and SCHO 842/9-2. Authors also would like to thank Bitop company for kind donation of SP enzyme.
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Abi, A., Wang, A. & Jördening, HJ. Continuous Laminaribiose Production Using an Immobilized Bienzymatic System in a Packed Bed Reactor. Appl Biochem Biotechnol 186, 861–876 (2018). https://doi.org/10.1007/s12010-018-2779-2
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DOI: https://doi.org/10.1007/s12010-018-2779-2