Table 1.
Carotenoid production in microorganisms using various metabolic engineering strategies.
| Major carotenoid | Host microorganism | Fermentation conditions | Yield (titer or/and content) | Metabolic engineering approach | Reference |
|---|---|---|---|---|---|
| Lycopene | Escherichia coli | Shake Flask | 448 mg/g | Regulation of lycopene synthesis pathway | Coussement et al. (2016) |
| Lycopene | Escherichia coli | Batch | 220 mg/L | Introduction of IUP | Chatzivasileiou et al. (2019) |
| Lycopene | Saccharomyces cerevisiae | Fed-batch | 2300 mg/L | Modular enzyme assembly | Kang et al. (2019) |
| β-carotene | Escherichia coli | Shake Flask | 44.2 mg/g | Increasing membrane synthesis | Wu et al. (2017) |
| β-carotene | Escherichia coli | Fed-batch | 2100 mg/L | Engineering central metabolic modules | Zhao et al. (2013) |
| β-carotene | Saccharomyces cerevisiae | Fed-batch | 2370 mg/L (73.3 mg/g) | Combined modular engineering | Ma et al. (2019a) |
| β-carotene | Yarrowia lipolytica | Fed-batch | 4000 mg/L | Iterative integration of multiple-copy pathway genes | Gao et al. (2017) |
| β-carotene | Yarrowia lipolytica | Fed-batch | 6500 mg/L (90 mg/g) | Optimization of promoter-gene pairs of crt | Larroude et al. (2018) |
| Astaxanthin | Corynebacterium glutamicum | Shake Flask | 1.7 mg/g | Screening different β-carotene hydroxylases | Henke et al. (2016) |
| Astaxanthin | Escherichia coli | Fed-batch | 385.0 mg/L (7.0 mg/g) | Membrane fused expression of β-carotene hydroxylase | Park et al. (2018a) |
| Astaxanthin | Escherichia coli | Fed-batch | 320 mg/L | Modular engineering | Zhang et al. (2018b) |