Maleate is one of the most important unsaturated four‐carbon dicarboxylic acids. It serves as an attractive building block in cosmetic, polymer, and pharmaceutical industries. Currently, industrial production of maleate relies mainly on chemical synthesis using benzene or butane as the starting materials under high temperature, which suffers from strict reaction conditions and low product yield. Here, we propose a novel biosynthetic pathway for maleate production in engineered Escherichia coli. We screened a superior salicylate 5‐hydroxylase that can catalyze hydroxylation of salicylate into gentisate with high conversion rate. Then, introduction of salicylate biosynthetic pathway and gentisate ring cleavage pathway allowed the synthesis of maleate from glycerol. Further optimizations including enhancement of precursors supply, disruption of competing pathways, and construction of a pyruvate recycling system, boosted maleate titer to 2.4 ± 0.1 g/L in shake flask experiments. Subsequent scale‐up biosynthesis of maleate in a 3‐L bioreactor under fed‐batch culture conditions enabled the production of 14.5 g/L of maleate, indicating a 268‐fold improvement compared with the titer generated by the wildtype E. coli strain carrying the entire maleate biosynthetic pathway. This study provided a promising microbial platform for industrial level synthesis of maleate, and demonstrated the highest titer of maleate production in microorganisms so far.
Carbon sources represent the most dominant cost factor in the industrial biomanufacturing of products. Thus, it has attracted much attention to seek cheap and renewable feedstocks, such as lignocellulose, crude glycerol, methanol and carbon dioxide, for biosynthesis of value-added compounds. Co-utilization of those carbon sources by microorganisms not only can reduce the production cost but also serves as a promising approach to improve the carbon yield. However, co-utilization of mixed carbon sources usually suffers from a low utilization rate. In the past few years, the development of metabolic engineering strategies to enhance carbon source co-utilization efficiency by inactivation of carbon catabolite repression has made significant progress. In this article, we provide informative and comprehensive insights into the co-utilization of two or more carbon sources including glucose, xylose, arabinose, glycerol and C1 compounds, and we put our focus on parallel utilization, synergetic utilization and complementary utilization of different carbon sources. Our goal is not only to summarize strategies of co-utilization of carbon sources, but also to discuss how to improve the carbon yield and the titer of target products.
α‐Aminoadipic acid (AAA) is a nonproteinogenic amino acid with potential applications in pharmaceutical, chemical and animal feed industries. Currently, AAA is produced by chemical synthesis, which suffers from high cost and low production efficiency. In this study, we engineered Escherichia coli for high‐level AAA production by coupling lysine biosynthesis and degradation pathways. First, the lysine‐α‐ketoglutarate reductase and saccharopine dehydrogenase from Saccharomyces cerevisiae and α‐aminoadipate‐δ‐semialdehyde dehydrogenase from Rhodococcus erythropolis were selected by in vitro enzyme assays for pathway assembly. Subsequently, lysine supply was enhanced by blocking its degradation pathway, overexpressing key pathway enzymes and improving nicotinamide adenine dineucleotide phosphate (NADPH) regeneration. Finally, a glutamate transporter from Corynebacterium glutamicum was introduced to elevate AAA efflux. The final strain produced 2.94 and 5.64 g/L AAA in shake flasks and bioreactors, respectively. This work provides an efficient and sustainable way for AAA production.
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