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Published on: May 18, 2020
Development of a multienzyme reactor for dopamine synthesis: II. Reactor engineering and simulation
W A Anderson1, M Moo-Young, R L Legge
1Biochemical Engineering Group, Department of Chemical Engineering, University of Waterloo, Waterloo, Ontario, Canada N2L 3G1.
This study developed a coimmobilized cell system for dopamine production using tyrosine phenol lyase (TPL) and tyrosine decarboxylase (TDC). Sequential reactions in a packed-bed reactor proved more efficient for dopamine synthesis than simultaneous ones.
Area of Science:
- Biochemical Engineering
- Enzyme Technology
- Biocatalysis
Background:
- Multienzyme reactions are crucial for synthesizing complex molecules.
- Optimizing reaction engineering for enzymatic processes is key to efficient biocatalysis.
- Dopamine synthesis involves sequential enzymatic steps.
Purpose of the Study:
- To investigate reaction engineering aspects of multienzyme systems for dopamine production.
- To coimmobilize microbial cells expressing tyrosine phenol lyase (TPL) and tyrosine decarboxylase (TDC).
- To evaluate the efficiency of sequential versus simultaneous reactions for dopamine synthesis.
Main Methods:
- Coimmobilization of Erwinia herbicola (TPL) and Streptococcus faecalis (TDC) in gelatin beads.
- Characterization of transport properties within the immobilized cell matrix.
- Packed-bed reactor studies for dopamine production.
- Computer simulations to compare sequential and simultaneous reaction strategies.
Main Results:
- Gelatin matrix showed minimal diffusion resistance for substrates and products.
- Dopamine exhibited partitioning into the gelatin matrix (K=2).
- Successful dopamine production was achieved in a packed-bed reactor, albeit with low conversion.
- Computer simulations indicated sequential reactions require smaller reactors for equivalent dopamine yield.
Conclusions:
- Coimmobilized microbial cells in gelatin beads are viable for multienzyme reactions.
- Sequential enzymatic reactions are more reactor-efficient for dopamine production compared to simultaneous reactions.
- Further optimization is needed to improve conversion rates in the packed-bed reactor system.
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