Model-Based Design of Biochemical Microreactors

被引:2
|
作者
Elbinger, Tobias [1 ]
Gahn, Markus [1 ]
Neuss-Radu, Maria [1 ]
Hante, Falk M. [2 ]
Voll, Lars M. [3 ]
Leugering, Guenter [2 ]
Knabner, Peter [1 ]
机构
[1] Friedrich Alexander Univ Erlangen Nurnberg, Chair Appl Math 1, Erlangen, Germany
[2] Friedrich Alexander Univ Erlangen Nurnberg, Chair Appl Math 2, Erlangen, Germany
[3] Friedrich Alexander Univ Erlangen Nurnberg, Chair Biochem, Erlangen, Germany
关键词
SYNTHETIC BIOLOGY; CELLS;
D O I
10.3389/fbioe.2016.00013
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Mathematical modeling of biochemical pathways is an important resource in Synthetic Biology, as the predictive power of simulating synthetic pathways represents an important step in the design of synthetic metabolons. In this paper, we are concerned with the mathematical modeling, simulation, and optimization of metabolic processes in biochemical microreactors able to carry out enzymatic reactions and to exchange metabolites with their surrounding medium. The results of the reported modeling approach are incorporated in the design of the first microreactor prototypes that are under construction. These microreactors consist of compartments separated by membranes carrying specific transporters for the input of substrates and export of products. Inside the compartments of the reactor multienzyme complexes assembled on nano-beads by peptide adapters are used to carry out metabolic reactions. The spatially resolved mathematical model describing the ongoing processes consists of a system of diffusion equations together with boundary and initial conditions. The boundary conditions model the exchange of metabolites with the neighboring compartments and the reactions at the surface of the nano-beads carrying the multienzyme complexes. Efficient and accurate approaches for numerical simulation of the mathematical model and for optimal design of the microreactor are developed. As a proof-of-concept scenario, a synthetic pathway for the conversion of sucrose to glucose-6-phosphate (G6P) was chosen. In this context, the mathematical model is employed to compute the spatio-temporal distributions of the metabolite concentrations, as well as application relevant quantities like the outflow rate of G6P. These computations are performed for different scenarios, where the number of beads as well as their loading capacity are varied. The computed metabolite distributions show spatial patterns, which differ for different experimental arrangements. Furthermore, the total output of G6P increases for scenarios where microcompartimentation of enzymes occurs. These results show that spatially resolved models are needed in the description of the conversion processes. Finally, the enzyme stoichiometry on the nano-beads is determined, which maximizes the production of glucose-6-phosphate.
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页数:13
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