TABLE 1.
Comparison of the 5AVA production by different engineered microbial strains and production of amino acids by B. methanolicus.
Organism | Approach | 5AVA titer [g l–1] | References |
Pseudomonas putida KT2440 | DavBA-based biocatalytic production of 5AVA from 30 g l–1 L-lysine | 20.80 | Liu et al., 2014 |
Corynebacterium glutamicum | Heterologous expression of davBA; sugar-based fed-batch fermentation | 33.10 | Shin et al., 2016 |
28.00 | Rohles et al., 2016 | ||
39.93 | Joo et al., 2017 | ||
Heterologous expression of ldcC and patAD; shake flask fermentation | 5.10 | Jorge et al., 2017 | |
Heterologous expression of puo and patD, deletion of gabTD; microbioreactor fermentation | 3.70 | Haupka et al., 2020 | |
Escherichia coli | Heterologous expression of davBA and deletion of cadA; glucose-based shaking flasks fermentation | 0.86 | Adkins et al., 2013 |
Heterologous expression of davBA; sugar-based fermentation; 10 g l–1 lysine provided | 3.60 | Park et al., 2013 | |
Heterologous expression of davBA; sugar-based fed-batch fermentation | 0.50 | Park et al., 2013 | |
Heterologous expression of davBA; glucose-based fed- batch fermentation; 120 g l–1 L-lysine provided | 90.59 | Park et al., 2014 | |
Heterologous expression of davBA; fed-batch whole-cell bioconversion of L-lysine maintained at 120 g l–1 | 240.70 | Wang et al., 2016 | |
Heterologous expression of raiP; whole-cell bioconversion; addition of 4% ethanol, 10 mM H2O2 and 100 g l–1 lysine | 29.12 | Cheng et al., 2018 | |
Heterologous expression of raiP; whole-cell bioconversion; 4% ethanol pretreatment, 10 mM H2O2 and 100 g l–1 lysine | 50.62 | Cheng et al., 2020 | |
Organism | Product in methanol-controlled fed-batch fermentation | Titer [g L–1] | References |
Bacillus methanolicus | L-Glutamate | 60.00 | Heggeset et al., 2012 |
L-Lysine | 11.00 | Brautaset et al., 2010 | |
γ-Aminobutyric acid | 9.00 | Irla et al., 2017 | |
Cadaverine | 11.30 | Nærdal et al., 2015 |