2020
DOI: 10.1016/j.bej.2020.107488
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Lycopene production from glucose, fatty acid and waste cooking oil by metabolically engineered Escherichia coli

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Cited by 45 publications
(43 citation statements)
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“…Lycopene production via various metabolic engineering optimization strategies in E. coli are summarized and listed in Table 1. Removal of competing pathways ∆gdhA, ∆aceE, ∆ytjC (gpmB), ∆fdhF 18 mg/g DCW Batch shake-flask cultivations [38] Pathway balancing Combination of gene knockout and overexpression 2.5 mg/g DCW - [20] Genome-wide stoichiometric flux balance analysis; genes knockouts 6.6 mg/g DCW Shake-flask fermentation [39] Gene knockout (∆hnr, ∆yliE) -Shake-flask fermentation [40] Regulatory engineering Ntr regulon, stimulated by excess glycolytic flux through sensing of ACP 0.16 mg/L/h Shake-flask fermentation [41] Engineering of the cAMP receptor protein (CRP) 18.49 mg/g DCW Batch fermentation [42] Optimization of carbon sources Auxiliary carbon source optimization 1050 mg/L Baffled flask fermentation [12] Supplementing auxiliary carbon sources 40 mg/L/h Fed-batch culture [43] Fermentation with fatty acids or waste cooking oils 94 mg/g DCW Fed-batch fermentation [44] Optimization of fermentation High cell density fermentation 220 mg/L Batch fermentation [45] Different types of plasmid expression; optimization of fermentation conditions 67 mg/g DCW Shake-flask fermentation [46] Targeted engineering Targeted engineering; targeted proteomic and intermediate analysis 1.23 g/L Fed-batch fermentation [47] Two-dimensional search for gene targets 16 mg/g DCW Shake-flask fermentation [48] Cofactor engineering…”
Section: The Primary Biosynthetic Pathways For Lycopene Productionmentioning
confidence: 99%
See 1 more Smart Citation
“…Lycopene production via various metabolic engineering optimization strategies in E. coli are summarized and listed in Table 1. Removal of competing pathways ∆gdhA, ∆aceE, ∆ytjC (gpmB), ∆fdhF 18 mg/g DCW Batch shake-flask cultivations [38] Pathway balancing Combination of gene knockout and overexpression 2.5 mg/g DCW - [20] Genome-wide stoichiometric flux balance analysis; genes knockouts 6.6 mg/g DCW Shake-flask fermentation [39] Gene knockout (∆hnr, ∆yliE) -Shake-flask fermentation [40] Regulatory engineering Ntr regulon, stimulated by excess glycolytic flux through sensing of ACP 0.16 mg/L/h Shake-flask fermentation [41] Engineering of the cAMP receptor protein (CRP) 18.49 mg/g DCW Batch fermentation [42] Optimization of carbon sources Auxiliary carbon source optimization 1050 mg/L Baffled flask fermentation [12] Supplementing auxiliary carbon sources 40 mg/L/h Fed-batch culture [43] Fermentation with fatty acids or waste cooking oils 94 mg/g DCW Fed-batch fermentation [44] Optimization of fermentation High cell density fermentation 220 mg/L Batch fermentation [45] Different types of plasmid expression; optimization of fermentation conditions 67 mg/g DCW Shake-flask fermentation [46] Targeted engineering Targeted engineering; targeted proteomic and intermediate analysis 1.23 g/L Fed-batch fermentation [47] Two-dimensional search for gene targets 16 mg/g DCW Shake-flask fermentation [48] Cofactor engineering…”
Section: The Primary Biosynthetic Pathways For Lycopene Productionmentioning
confidence: 99%
“…Similarly, in another study, the MVA lower pathway was introduced into E. coli, in which glycerol was supplied as the carbon source with addition of mevalonate, and Tween 80 was added to prevent clump formation, resulting in a significant increase in lycopene production [54]. Moreover, an engineered E. coli strain introduced with the fatty acid transport system was capable of utilizing free fatty acids or waste cooking oil to produce lycopene, with the highest yield of 94 mg/g [44].…”
Section: Optimization Of Auxiliary Carbon Source and Fermentation Modesmentioning
confidence: 99%
“…For example, when obtained from palm industry byproducts, the average carbon price per ton of palmitic acid is about $35 per ton of C (calculated from $570 per ton of palmitic acid extract), which is much lower than the average carbon price for glucose ($46 per ton of C, calculated from $275 per ton of glucose) [27]. In previous studies, we have successfully developed efficient routes to produce target chemicals, such as 3-hydroxypropionic acid and lycopene, in high yields from fatty acids [28,29].…”
Section: Introductionmentioning
confidence: 99%
“…For example, when obtained from palm industry byproducts, the average carbon price per ton of palmitic acid is about $35 per ton of C (calculated from $570 per ton of palmitic acid extract), which is much lower than the average carbon price for glucose ($46 per ton of C, calculated from $275 per ton of glucose) [27]. In previous studies, we have successfully developed e cient routes to produce target chemicals, such as 3-hydroxypropionic acid and lycopene, in high yields from fatty acids [28,29].…”
Section: Introductionmentioning
confidence: 99%