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Background: Predictable control of gene expression is necessary for the rational design and optimization of cell factories. In the yeast Saccharomyces cerevisiae, the promoter is one of the most important tools available for controlling gene expression. However, the complex expression patterns of yeast promoters have not been fully characterised and compared on different carbon sources (glucose, sucrose, galactose and ethanol) and across the diauxic shift in glucose batch cultivation. These conditions are of importance to yeast cell factory design because they are commonly used and encountered in industrial processes. Here, the activities of a series of "constitutive" and inducible promoters were characterised in single cells throughout the fermentation using green fluorescent protein (GFP) as a reporter. Results: The "constitutive" promoters, including glycolytic promoters, transcription elongation factor promoters and ribosomal promoters, differed in their response patterns to different carbon sources; however, in glucose batch cultivation, expression driven by these promoters decreased sharply as glucose was depleted and cells moved towards the diauxic shift. Promoters induced at low-glucose levels (PHXT7, PSSA1 and PADH2) varied in induction strength on non-glucose carbon sources (sucrose, galactose and ethanol); in contrast to the "constitutive" promoters, GFP expression increased as glucose decreased and cells moved towards the diauxic shift. While lower than several "constitutive" promoters during the exponential phase, expression from the SSA1 promoter was higher in the post-diauxic phase than the commonly-used TEF1 promoter. The galactose-inducible GAL1 promoter provided the highest GFP expression on galactose, and the copper-inducible CUP1 promoter provided the highest induced GFP expression following the diauxic shift. Conclusions: The data provides a foundation for predictable and optimised control of gene expression levels on different carbon sources and throughout batch fermentation, including during and after the diauxic shift. This information can be applied for designing expression approaches to improve yields, rates and titres in yeast cell factories. [ABSTRACT FROM AUTHOR]

Sucrose is one of the most promising carbon sources for industrial fermentation. To achieve sucrose catabolism, the sucrose utilization operons have been introduced into microorganisms that are not able to utilize sucrose. However, the rates of growth and sucrose uptake of these engineered strains were relatively low to be successfully employed for industrial applications. Here, we report a practical example of developing sucrose-utilizing microorganisms using Escherichia coli K-12 as a model system. The sucrose utilizing ability was acquired by introducing only β-fructofuranosidase from three different sucrose-utilizing organisms ( Mannheimia succiniciproducens, E. coli W, and Bacillus subtilis). Among them, the M. succiniciproducens β-fructofuranosidase was found to be the most effective for sucrose utilization. Analyses of the underlying mechanism revealed that sucrose was hydrolyzed into glucose and fructose in the extracellular space and both liberated hexoses could be transported by their respective uptake systems in E. coli K-12. To prove that this system can also be applied for the production of useful metabolites, the M. succiniciproducens β-fructofuranosidase was introduced into the engineered l-threonine production strain of E. coli K-12. This recombinant strain was able to produce 51.1 g/L l-threonine by fed-batch culture, resulting in an overall yield of 0.284 g l-threonine per g sucrose. This simple approach to make E. coli K-12 to acquire sucrose-utilizing ability and its successful biotechnological application can be employed to develop sustainable bioprocesses using renewable biomass. [ABSTRACT FROM AUTHOR]

Sesquiterpenes are C15 isoprenoids with utility as fragrances, flavours, pharmaceuticals, and potential biofuels. Microbial fermentation is being examined as a competitive approach for bulk production of these compounds. Competition for carbon allocation between synthesis of endogenous sterols and production of the introduced sesquiterpene limits yields. Achieving balance between endogenous sterols and heterologous sesquiterpenes is therefore required to achieve economical yields. In the current study, the yeast Saccharomyces cerevisiae was used to produce the acyclic sesquiterpene alcohol, trans-nerolidol. Nerolidol production was first improved by enhancing the upstream mevalonate pathway for the synthesis of the precursor farnesyl pyrophosphate (FPP). However, excess FPP was partially directed towards squalene by squalene synthase (Erg9p), resulting in squalene accumulation to 1% biomass; moreover, the specific growth rate declined. In order to re-direct carbon away from sterol production and towards the desired heterologous sesquiterpene, a novel protein destabilisation approach was developed for Erg9p. It was shown that Erg9p is located on endoplasmic reticulum and lipid droplets through a C-terminal ER-targeted transmembrane peptide. A PEST (rich in Pro, Glu/Asp, Ser, and Thr) sequence-dependent endoplasmic reticulum-associated protein degradation (ERAD) mechanism was established to decrease cellular levels of Erg9p without relying on inducers, repressors or specific repressing conditions. This improved nerolidol titre by 86% to ~100 mg L −1 . In this strain, squalene levels were similar to the wild-type control strain, and downstream ergosterol levels were slightly decreased relative to the control, indicating redirection of carbon away from sterols and towards sesquiterpene production. There was no negative effect on cell growth under these conditions. Protein degradation is an efficient mechanism to control carbon allocation at flux-competing nodes in metabolic engineering applications. This study demonstrates that an engineered ERAD mechanism can be used to balance flux competition between the endogenous sterol pathway and an introduced bio-product pathways at the FPP node. The approach of protein degradation in general might be more widely applied to improve metabolic engineering outcomes. [ABSTRACT FROM AUTHOR]

Abstract: Sucrose has economic and environmental advantages over glucose as a feedstock for bioprocesses. E. coli is widely used in industry, but the majority of current industrial E. coli strains cannot utilize sucrose. Previous attempts to transfer sucrose catabolic capabilities into non-sucrose-utilizing strains have met with limited success due to low growth rates on sucrose and phenotypic instability of the engineered strains. To address these problems, we developed a transferrable sucrose utilization cassette which confers efficient sucrose catabolism when integrated onto the E. coli chromosome. The cassette was based on the csc genes from E. coli W, a strain which grows very quickly on sucrose. Both plasmid-borne expression and chromosomal integration of a repressor-less sucrose utilizing cassette were investigated in E. coli strains K-12, B and C. In contrast to previous studies, strains harboring chromosomal cassettes could grow at the same rate as they do on glucose. Interestingly, we also discovered that spontaneous chromosomal integration of the csc genes was required to allow efficient growth from plasmid-transformed strains. The ability to engineer industrial strains for efficient sucrose utilization will allow substitution of sucrose for glucose in industrial fermentations. This will encourage the use of sucrose as a carbon source and assist in transition of our petrochemical-based economy to a bio-based economy. [Copyright &y& Elsevier]

Abstract: Sucrose has several advantages over glucose as a feedstock for bioprocesses, both environmentally and economically. However, most industrial Escherichia coli strains are unable to utilize sucrose. E. coli W can grow on sucrose but stops growing when sucrose concentrations become low. This is undesirable in fed-batch conditions where sugar levels are low between feeding pulses. Sucrose uptake rates were improved by removal of the cscR gene, which encodes a protein that represses expression of the sucrose utilization genes at low sucrose concentrations. Poly-3-hydroxybutyrate (PHB) was used as a model compound in order to assess the effect of improved sugar utilization on bio-production. In the cscR knockout strain, production from sucrose was improved by 50%; this strain also produced 30% more PHB than the wild-type using glucose. This result demonstrates the feasibility of utilizing sucrose as an industrial feedstock for E. coli-based bioprocesses in high cell density culture. [Copyright &y& Elsevier]