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Saccharomyces cerevisiae is the workhorse of fermentation industry. Upon engineering for D-lactate production by a series of gene deletions, this yeast had deficiencies in cell growth and D-lactate production at high substrate concentrations. Complex nutrients or high cell density were thus required to support growth and D-lactate production with a potential to increase medium and process cost of industrial-scale D-lactate production. As an alternative microbial biocatalyst, a Crabtree-negative and thermotolerant yeast Kluyveromyces marxianus was engineered in this study to produce high titer and yield of D-lactate at a lower pH without growth defects. Only pyruvate decarboxylase 1 (PDC1) gene was replaced by a codon-optimized bacterial D-lactate dehydrogenase (ldhA). Ethanol, glycerol, or acetic acid was not produced by the resulting strain, KMΔpdc1::ldhA. Aeration rate at 1.5 vvm and culture pH 5.0 at 30 °C provided the highest D-lactate titer of 42.97 ± 0.48 g/L from glucose. Yield and productivity of D-lactate, and glucose-consumption rate were 0.85 ± 0.01 g/g, 0.90 ± 0.01 g/(L·h), and 1.06 ± 0.00 g/(L·h), respectively. Surprisingly, D-lactate titer, productivity, and glucose-consumption rate of 52.29 ± 0.68 g/L, 1.38 ± 0.05 g/(L·h), and 1.22 ± 0.00 g/(L·h), respectively, were higher at 42 °C compared to 30 °C. Sugarcane molasses, a low-value carbon, led to the highest D-lactate titer and yield of 66.26 ± 0.81 g/L and 0.91 ± 0.01 g/g, respectively, in a medium without additional nutrients. This study is a pioneer work of engineering K. marxianus to produce D-lactate at the yield approaching theoretical maximum using simple batch process. Our results support the potential of an engineered K. marxianus for D-lactate production on an industrial scale. Key points: • K. marxianus was engineered by deleting PDC1 and expressing codon-optimized D-ldhA. • The strain allowed high D-lactate titer and yield under pH ranging from 3.5 to 5.0. • The strain produced 66 g/L D-lactate at 30 °C from molasses without any additional nutrients. [ABSTRACT FROM AUTHOR]

The methylotrophic yeast Pichia pastoris (syn. Komagataella phaffii) is a successful host widely used in recombinant protein production. The widespread use of a methanol‐regulated alcohol oxidase 1 (AOX1) promoter for recombinant protein production has directed studies particularly about methanol metabolism in this yeast. Although there is comprehensive knowledge about methanol metabolism, there are other mechanisms in P. pastoris that have not been investigated yet, such as ethanol metabolism. The gene responsible for the consumption of ethanol ADH2 (XM_002491337, known as ADH3) was identified and characterized in our previous study. In this study, the ADH genes (XM_002489969, XM_002491163, XM_002493969) in P. pastoris genome were investigated to determine their roles in ethanol production by gene disruption analysis. We report that the ADH900 (XM_002491163) is the main gene responsible for ethanol production in P. pastoris. The ADH2 gene, previously identified as the only gene responsible for ethanol consumption, also plays a minor role in ethanol production in the absence of the ADH900 gene. The investigation of the carbon source regulation mechanism has also revealed that the ADH2 gene exhibit similar expression behaviours with ADH900 on glucose, glycerol, and methanol, however, it is strongly induced by ethanol. [ABSTRACT FROM AUTHOR]

Many natural drugs use acetyl-CoA as the key biosynthetic precursor. While in eukaryotic chassis host like yeast, efficient biosynthesis of these drugs is often hampered by insufficient acetyl-CoA supply because of its compartmentalized metabolism. Reported acetyl-CoA engineering commonly modifies central carbon metabolism to pull and push acetyl-CoA into cytosol from sugars or redirects biosynthetic pathways in organelles, involving complicated metabolic engineering strategies. We constructed a new biosynthetic system based on a Crabtree-negative yeast, which grew exceptionally on ethanol and assimilated ethanol directly in cytosol to acetyl-CoA (3 steps). A glucose-repressed and ethanol-induced transcriptional signal amplification device (ESAD) with 20-fold signal increase was constructed by rewiring native transcriptional regulation circuits. This made ethanol the sole and fast-growing substrate, acetyl-CoA precursor, and strong biosynthetic pathway inducer simultaneously. The ESAD was used for biosynthesis of a commercial hypolipidemic drug intermediate, monacolin J. A strain producing dihydromonacolin L was firstly constructed and systematically engineered. We further developed a coculture system equipped with this upstream strain and a downstream strain with dihydromonacolin L–to–monacolin J module controlled by a synthetic constitutive transcriptional signal amplification device (CSAD). It produced a high monacolin J titre of 2.2 g/L on ethanol in bioreactor. Engineering glucose-supported and ethanol-repressed fatty acids biosynthesis in the upstream strain contributed more acetyl-CoA for monacolin J and improved its titre to 3.2 g/L, far surpassing other reported productions in yeasts. This study provides a new paradigm for facilitating the high-yield production of acetyl-CoA derived pharmaceuticals and value-added molecules. Image 1 • Efficient ethanol–to–acetyl-CoA metabolism supported fast growth of P. pastoris. • Engineered yeast uses ethanol as sole carbon source, precursor and strong inducer. • Dihydromonacolin L biosynthesis driven by the ESAD device reached high yield. • Engineered ethanol assimilation and fatty acids biosynthesis improved DML formation. • Coculture system with the devices of ESAD and CSAD led to high titres of monacolin J. [ABSTRACT FROM AUTHOR]

Background: The methylotrophic, Crabtree-negative yeast Pichia pastoris is widely used as a heterologous protein production host. Strong inducible promoters derived from methanol utilization genes or constitutive glycolytic promoters are typically used to drive gene expression. Notably, genes involved in methanol utilization are not only repressed by the presence of glucose, but also by glycerol. This unusual regulatory behavior prompted us to study the regulation of carbon substrate utilization in different bioprocess conditions on a genome wide scale. Results: We performed microarray analysis on the total mRNA population as well as mRNA that had been fractionated according to ribosome occupancy. Translationally quiescent mRNAs were defined as being associated with single ribosomes (monosomes) and highly-translated mRNAs with multiple ribosomes (polysomes). We found that despite their lower growth rates, global translation was most active in methanol-grown P. pastoris cells, followed by excess glycerol- or glucose-grown cells. Transcript-specific translational responses were found to be minimal, while extensive transcriptional regulation was observed for cells grown on different carbon sources. Due to their respiratory metabolism, cells grown in excess glucose or glycerol had very similar expression profiles. Genes subject to glucose repression were mainly involved in the metabolism of alternative carbon sources including the control of glycerol uptake and metabolism. Peroxisomal and methanol utilization genes were confirmed to be subject to carbon substrate repression in excess glucose or glycerol, but were found to be strongly de-repressed in limiting glucose-conditions (as are often applied in fed batch cultivations) in addition to induction by methanol. Conclusions: P. pastoris cells grown in excess glycerol or glucose have similar transcript profiles in contrast to S. cerevisiae cells, in which the transcriptional response to these carbon sources is very different. The main response to different growth conditions in P. pastoris is transcriptional; translational regulation was not transcript-specific. The high proportion of mRNAs associated with polysomes in methanol-grown cells is a major finding of this study; it reveals that high productivity during methanol induction is directly linked to the growth condition and not only to promoter strength. [ABSTRACT FROM AUTHOR]