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Updated: Sep 21, 2025

In Vivo Monitoring of Transcriptional Activity During Metabolic Transition Using a Bioluminescent Reporter in Yeast
Published on: February 21, 2025
Metabolic engineering of the malonyl-CoA pathway to efficiently produce malonate in Saccharomyces cerevisiae
Shiyun Li1, Wenxuan Fu2, Ruifang Su2
1National Engineering Research Center of Cereal Fermentation and Food Biomanufacturing, Jiangnan University, 1800 Lihu Road, Wuxi, Jiangsu, 214122, China.
Abstract:
Malonate is a platform chemical that has been utilized to synthesize many valuable chemical compounds. Here, Saccharomyces cerevisiae was metabolically engineered to produce malonate through the malonyl-CoA pathway. To construct the key step of converting malonyl-CoA to malonate, a native mitochondrial 3-hydroxyisobutyryl-CoA hydrolase gene EHD3 was mutated to target the cytoplasm and obtain malonyl-CoA hydrolase activity. The malonyl-CoA hydrolase activity of Ehd3 was achieved by mutating the malonyl-CoA binding site F121 to I121 and the active site E124 to seven amino acids (S/T/H/K/R/N/Q). We identified that the strain with E124S mutation had the highest malonate titer with 13.6 mg/L. Genomic integration of the mutant EHD3 and ACC1** to delta sequence sites was further explored to increase their reliable expression. Accordingly, a screening method with the work flow of fluorescence detection, shake-tube fermentation, and shake-flask fermentation was constructed to screen high copy delta sequences efficiently. The malonate titer was improved to 73.55 mg/L after screening the ∼1500 integrative strains, which was increased 4.4-folds than that of the episomal strain. We further engineered the strain by regulating the expression of key enzyme in the malonyl-CoA pathway to improve the precursor supply and inhibiting its competing pathways, and the final engineered strain LMA-16 produced 187.25 mg/L in the flask, 14-fold compared with the initial episomal expression strain. Finally, the combined efforts increased the malonate titer to 1.62 g/L in fed-batch fermentation.
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