From: Metabolic engineering of microorganisms for production of aromatic compounds
Host | Product | Precursor | Carbon source | Titer | Time (h) | Bioprocess strategy | Systems metabolic engineering strategies | References |
---|---|---|---|---|---|---|---|---|
E. coli | PHBA | CHR | Glucose | 12Â g/L | 72 | Fed-batch (fermenter) | Overexpressing ubiC and particular genes in PP and SHK pathway | [25] |
cis, cis-Muconic acid | DHS | Glucose | 36.8Â g/L | 48 | Fed-batch (fermenter, 2Â L) | Inserting three heterologous genes from different microorganisms, being responsible for the product synthesis, deleting SDH-coding gene | [38] | |
AA | Glycerol/glucose | 0.389Â g/L | 32 | Batch (shake flask) | Optimizing AA pathway through overexpressing genes in PP and SHK pathway and shunting tryptophan biosynthesis; screening target genes being responsible for the biosynthesis from AA | [40] | ||
2,3-DHBA | Glycerol/glucose | 0.480Â g/L | 48 | Batch (shake flask) | Screening and characterization of new BDC enzyme from different organisms; overexpressing target genes; deleting gene responsible for degradation of 2,3-DHBA | [41] | ||
4HBA | Glucose | 0.170 g/L | 24 | Batch (shake flask) | Integrating heterologous genes for the synthesis of CMA from precursor 4HBA to target product; over- and co-expressing native target genes and mutated ones; deleting genes in PEP–PTS | [42] | ||
SA | Glycerol/glucose | 1.5Â g/L | 48 | Batch (shake flask) | Shunting SHK pathway from chorismate to aromatic amino acids; overexpressing genes in CCM and SHK pathway; Integrating heterologous genes being responsible in SA anabolism and catabolism | [43] | ||
Salicylic acid | CHA | Glycerol/glucose | 1.2Â g/L | 48 | Batch (shake flask) | |||
CHA | Glucose | 11.5Â g/L | 48 | Batch (fermenter, 2Â L) | Replacing endogenous PTS system; Deleting genes of enzyme converting PEP to PYR; Integrating genes catalyzing product formation via CHR | [64] | ||
PABA | CHA | Glucose | 4.8Â g/L | 48 | Fed-batch (shake flask) | Overexpressing feedback resistance gene at entrance of SHK pathway and heterologous genes; the integration of fused type ADC synthase | [70] | |
Gallic acid | DHS | Glucose | 20Â g/L | 48 | Fed-batch (fermenter) | Discovering side activity of pobA mutant to produce gallic acid from protocatechuic acid. | [73] | |
Pyrogallol | 2,3-DHBA | 2,3-DHBA | 0.893Â g/L | 24 | Fed-batch (shake-flask) | Identifying and characterizing 2,3-DHBA MNX1 from different sources; Integrating nahG-encoded MNX1; Optimizing CCM and SHK pathway with EntCBA activity | [74] | |
1.04Â g/L | Autoxidation with oxygen scavenging agent ascorbic acid into the medium | |||||||
Gallic acid | PHBA | Glucose/glycerol | 1.266Â g/L | 36 | Batch (shake-flask) | Mutating pobA (Y385F/T294A) from Pseudomonas aeruginosa; step-wise upstream pathway engineering with overexpression of UbiC to increase carbon flux to precursor | [75] | |
Quinic acid | DHQ | Glucose | 4.8Â g/L | N.A | Batch (shake-flask) | Integration of gene encoding quinic acid dehydrogenase in Klebsiella pneumaniae | [76] | |
Glucose | 49Â g/L | 48 | Fed-batch (fermenter, 2Â L) | Integration of aroE encoded shikimate dehydrogenase | [77] | |||
PDC | DHS | Glucose | 16.72Â g/L | 60 | Fed-batch (fermenter, 6.6 L) | Overexpressing feedback resistant variant aroG, ppsA and shiA; Integrating three heterologous genes | [39] | |
C. glutamicum | PHBA | CHA | Glucose | 36.6Â g/L | 24 | Growth arrested bioprocess (fermenter, 1Â L) | Deleting target genes in competing pathway in CCM and SHK pathway; Screening and introducing best ubiC-encoded enzyme; Stepwise overexpressing the genes in PP and SHK pathway | [26] |
PABA | CHA | Glucose | 43Â g/L | 48 | Fed-batch (fermenter, 1Â L) | Screening pab genes from different microorganisms for target synthesis; Introducing fused ADC synthase from C. callunae and ADC4 lyase from X. bovienii | [71] | |
P. putida | cis, cis-Muconic acid | DHS | Glucose | 4.92Â g/L | 54 | Fed-batch (fermenter, 0.5Â L) | Co-expression of two-genetically associated protein with PCA decarboxylase | [46] |
S. cerevisiae | PHBA | CHA | Glucose | 0.089 g/L | > 150 | Pulse-feeding (fermenter, 1 L) | Deleting target genes for alleviated negative feedback; integration and overexpression of chorismate lyase originated from E. coli | [28] |
Glucose | 0.148Â g/L | N.A | Batch (shake flask) | Quorum sensing linked RNA interference for separate growth and production phase | [29] | |||
cis, cis-Muconic acid | DHS | Glucose | 1.56 mg/L | 170 | Batch (shake flask) | Screening and combining best candidates of heterologous genes s catalyzing the reactions from DHS to cis–cis muconic acid | [44] | |
Glucose | 141Â mg/L | 108 | Batch (shake flask) | Screening and combining target genes and their putative concerned with targeted product; overexpressing PP pathway specific gene and feedback resistant mutant gene in SHK pathway | [45] | |||
PABA | CHA | Glucose | 0.034 g/L | > 150 | Pulse-feeding (fermenter, 1 L) | Eliminating the genes on the entry towards aromatic amino acid pathway; overproducing gene related to product | [28] | |
Glucose | > 0.068 g/L | 130 | Batch (shake flask) | Screening additional allels of target homologous 2 genes being responsible for PABA production; combining them each other for their overexpression | [69] | |||
Glycerol | 0.215Â g/L | Fed-batch (fermenter) |