Enhancement of cloned gene product synthesis via autoselection in recombinant Saccharomyces cerevisiae

Saccharomyces cerevisiae autoselection strains with mutations in the ura3, fur1, and urid-k genes have been obtained through a sequential isolation procedure. This autoselection system is an extension of one described by Loison et al. The mutations effectively block both the pyrimidine biosynthetic and salvage pathways and in combination are lethal to the host. Therefore, a plasmidencoded URA3 gene is essential for cell viability regardless of the growth conditions, and complex (traditionally nonselective) media can be employed without the risk of plasmid loss. The effects of medium enrichment on growth and cloned gene product synthesis were examined in batch culture for two autoselection strains. The plasmid gene product beta-galactosidase was under the control of the yeast GAL1 promoter, and two methods of induction were employed; one strain was induced via temperature shift while the other was induced by galactose addition. Three nutrient media were investigated: a lean selective medium (SD), a richer semidefined medium (SDC), and a rich complex medium (YPD). The results demonstrated the improvements in cloned gene productivity possible when the growth medium is enriched, with up to 10-fold increases in beta-galactosidase productivity observed. Plasmid instability and mutation reversion were not problems for the autoselection strains, even in uracil-containing medium. Short-term plasmid stabilities were approximately 90% in all three media tested. During continuous culture of the autoselection temperature-sensitive strain, long-term plasmid stability was excellent and beta-galactosidase expression remained high after more than 25 residence times under inducing conditions. In contrast, both beta-galactosidase specific activity and plasmid stability decreased linearly with time for an analogous nonautoselection strain. The introduced fur1 and uridk mutations were very stable; after more than 50 generations of growth in complex medium, stability values of 99-100% were measured. (c) 1993 Wiley & Sons, Inc.     

An autoselection system in recombinant Kluyveromyces lactis enhances cloned gene stability and provides freedom in medium selection

An autoselection system for increasing plasmid stability in Kluyveromyces lactis, based on the blockage of the pyrimidine de novo and salvage pathways, was investigated. In a manner analogous to that used in Saccharomyces cerevisiae, a putative “fur1” mutation was selected in a uraA K. lactis strain using 5-fluorouracil and 5-fluorocytosine plates. Survival of the mutant required expression of a plasmid-borne URA3 gene regardless of the culture medium employed, verifying the efficacy of this autoselection system in K. lactis. The expression of heterologous invertase, encoded by the S. cerevisiae SUC2 gene, was studied during long-term sequential batch cultures (70 generations) in complex yeast/peptone/glucose medium. The fur1 mutant successfully retained the plasmid; invertase specific activity remained above 90% of the initial level. Furthermore, no mutation reversion was observed. In contrast, for the control non-fur1 strain, only 4% of the cells retained the plasmid after 70 generations, and invertase specific activity dropped to less than 10% of the initial level. Experiments comparing growth and activity in different media indicated the potential for improving productivity through medium enrichment using this autoselection system. Received: 1 April 1997 / Received revision: 16 August 1997 / Accepted: 11 September 1997     

Partial-pKD1 plasmids provide enhanced structural stability for heterologous protein production in Kluyveromyces lactis

The stability of pKD1-based vectors in the yeast Kluyveromyces lactis was investigated during short- and long-term culture. The vectors carried an expression/secretion cassette consisting of the Saccharomyces cerevisiaeSUC2 gene under the control of the S. cerevisiaeα-factor promoter and leader. The first set of vectors contained the entire pKD1 sequence linearized at either the unique EcoRI or the unique SphI site of the pKD1 plasmid. During long-term sequential batch culture in selective medium with either vector, invertase activity rapidly dropped while the plasmid-bearing population increased from 60% to 100%. This apparently contradictory behavior was due to structural instability. The enzyme restriction patterns of recovered plasmid DNA retained the pKD1 band while the band containing the SUC2 cassette had decreased substantially in size. To overcome this structural instability, a vector carrying the pKD1 replication origin and the cis-acting stability locus (lacking the inverted repeats) was employed in a pKD1⁺ (but otherwise isogenic) strain. With this plasmid, invertase activity remained constant (for at least 70 generations). While the new vector was significantly more stable, initial invertase activity was substantially lower than that for the vectors containing the full pKD1 sequence. Southern hybridization confirmed that this decrease was primarily due to reduced copy number. The results indicate that full-pKD1 vectors may be preferred for batch culture, while partial-pKD1 vectors are more suitable for long-term (e.g. fed-batch or continuous) culture. Received: 24 June 1997 / Received revision: 14 November 1997 / Accepted: 29 November 1997     

Overexpression of <Emphasis Type="Italic">ADH1</Emphasis> and <Emphasis Type="Italic">HXT1</Emphasis> genes in the yeast <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> improves the fermentative efficiency during tequila elaboration

This work assessed the effect of the overexpression of ADH1 and HXT1 genes in the Saccharomyces cerevisiae AR5 strain during fermentation of Agave tequilana Weber blue variety must. Both genes were cloned individually and simultaneously into a yeast centromere plasmid. Two transformant strains overexpressing ADH1 and HXT1 individually and one strain overexpressing both genes were randomly selected and named A1, A3 and A5 respectively. Overexpression effect on growth and ethanol production of the A1, A3 and A5 strains was evaluated in fermentative conditions in A. tequilana Weber blue variety must and YPD medium. During growth in YPD and Agave media, all the recombinant strains showed lower cell mass formation than the wild type AR5 strain. Adh enzymatic activity in the recombinant strains A1 and A5 cultivated in A. tequilana and YPD medium was higher than in the wild type. The overexpression of both genes individually and simultaneously had no significant effect on ethanol formation; however, the fermentative efficiency of the A5 strain increased from 80.33% to 84.57% and 89.40% to 94.29% in YPD and Agave medium respectively.     

Standard YPD, even supplemented with extra nutrients, does not always compensate growth defects of Saccharomyces cerevisiae auxotrophic strains

Conventional complex media are routinely used to grow auxotrophic strains under the assumption that they can compensate the latter's nutritional deficiencies. We here demonstrate that this is not always true. This study compares the growth parameters of Saccharomyces cerevisiae (S288C) and its derived auxotrophic strains FY1679-14C and BY4741 in synthetic minimal medium (SD), standard YPD medium from two of the most commonly used suppliers, or modified YPD medium. Maximum specific growth rates of auxotrophic strains were slightly lower than the prototrophic case in all growth conditions tested. Also, the biomass production of auxotrophic strains in synthetic medium was slightly less than the prototrophic case. However in both of the two standard YPD media used, the biomass production of both auxotrophic strains was markedly lower than that of the prototrophic one. The extent of the differences depended on the medium used. Indeed in one of the two YPD media, the lower biomass production of auxotrophic strains was evident even at the diauxic shift. Uracil seems to be the main limiting growth factor for both auxotrophic strains growing in the two standard YPD medium tested. No YPD media or specific supplement was able to compensate for the effect of the auxotrophic mutations in the multiple auxotrophic marker strain BY4741. The fact that auxotrophic strains grew poorly on YPD when compared to their prototrophic counterpart indicates that standard YPD medium is not sufficient to overcome the effect of auxotrophic mutations.     

Localization of cloned invertase in Saccharomyces cerevisiae directed by the SUC2 and MFalpha1 signal sequences

Protein localization in Saccharomyces cerevisiae was studied with two plasmid systems used as a model: one containing the SUC2 structural gene fused with the MFalpha1 (alpha-factor) promoter and signal-sequence, the other containing the entire SUC2 gene. Special emphasis was placed on the effect of promoter/signal-sequence (SUC2 vs. MFalpha1) on the efficiency of invertase transport. The MFalpha 1 and SUC2 signal sequences were capable of transporting, respectively, 83% and 77% of cloned invertase out of the cytoplasm. However, the SUC2 promoter was easier to control since a six-fold enhancement of the transported invertase activity associated with derepression was achieved in response to a glucose concentration change from 10 to 2 g/L Cloning on a multicopy plasmid resulted in a four-fold increase in total specific invertase activity over the wild type yeast strain (which harbors a single copy of the SUC2 gene on the chromosome), whereas the chromosomal site was more efficient for invertase localization yielding over 90% of the invertase transported out of the cytoplasm. Transient experiments done with the SUC2 signal-sequence-containing plasmid showed that the specific invertase activity in the periplasmic space reached a maximum three hours after derepression, then decreased very slowly with an accompanying gradual increase in invertase activity in the growth medium.     

A chemostat culture as a tool for the improvement of a recombinant E. coli strain over-producing penicillin G acylase

The recombinant strain RE3(pKA18) of Escherichia coli constitutively overproduces penicillin G acylase (PGA) from plasmid-borne gene pga. The host strain RE3 bears the same pga gene on its chromosome, the expression of which is controlled by the natural mechanism of induction with phenylacetic acid (PA). To evaluate the maximum biosynthetic capacity for PGA, induction of the chromosomal pga by PA was studied in a culture of the recombinant strain. PGA production by batch cultures of RE3(pKA18) and RE3 showed a different response to the addition of PA to the medium: while an addition of PA induces PGA in a culture of strain RE3 as expected, in recombinant cells it lowers the specific activity of PGA and a large amount of PGA is released into the culture medium. To improve the PGA production, the strain RE3(pKA18) was cultured in a carbon-limited chemostat and subjected to selection pressure in a medium supplemented with phenylacetic acid amide (PAA). Phenylacetic acid amide served as a source of nitrogen, an inducer of PGA and a factor exerting positive selection pressure on the maintenance of the recombinant plasmid. After 130 generations of growth in the presence of the inducer, no recombinant strain with constitutive expression of the chromosomal gene pga was detected in the prevailing P(+) subpopulation in the chemostat. Shake-flask experiments with the parent recombinant strain RE3(pKA18), host strain RE3, chemostat evolvant ERE3(epKA18), the cured host ERE3 alone, and its derivative after retransformation with ancestral plasmid ERE3(pKA18) showed that inactivation of the plasmid-borne pga by a frame-shift mutation (plasmid epKA18) occurred in the plasmid-bearing subpopulation accumulated in the chemostat. Marked adaptive changes evolved in the host ERE3 during a 130 generation culture: (1) the specific growth rate of the host increased by 30% in a medium without PA, (2) the copy number of plasmids pKA18 and epKA18 in the host cultured in PA-free medium dropped by about 40%, and (3) the leakage of PGA from the cell in the presence of PA found in strain RE3(pKA18) was not observed in strain ERE3(pKA18). This new recombinant strain with modified traits was constructed by means of retransformation of the evolved host ERE3 with ancestral plasmid pKA18.     

Isolation of an osmotolerant ale strain of Saccharomyces cerevisiae

Saccharomyces cerevisiae (ale strain) grown in batch culture to stationary phase was tested for its tolerance to heat (50 degrees C for 5 min), hydrogen peroxide (0.3 M) and salt (growth in 1.5 M sodium chloride/YPD medium). Yeast cells which have been exposed previously to heat shock are more tolerant to hydrogen peroxide and high salt concentrations (1.5 M NaCl) than the controls. Their fermentative activity as judged by glucose consumption and their viability, as judged by cell number and density have higher levels when compared with cells not previously exposed to heat shock. Experimental conditions facilitated the isolation of S. cerevisiae ale strain, which was tolerant to heat, and other agents such as hydrogen peroxide and sodium chloride.     

High-level expression of a fungal pyranose oxidase in high cell-density fed-batch cultivations of Escherichia coli using lactose as inducer

Expression of a recombinant pyranose oxidase (P2O) from the basidiomycete Trametes ochracea has been increased 10-fold in shaking flask cultures of Escherichia coli BL21(DE3) harboring plasmid pSE33 by optimizing the composition of the culture medium using an experimental design approach. Inexpensive lactose was used as a medium component and inducer of expression of the P2O gene, which is under the control of a trc promoter. The expression system was studied in detail in batch and fed-batch cultivations with the aim to improve the expression level of active recombinant protein and to minimize the formation of inclusion bodies. In batch cultivations, the highest specific P2O activity of 0.9 U (mg of soluble protein)(-1) was measured in oxygen-limited cultures grown at 25 degrees C. The highest overall volumetric productivity of 33 mg of active P2O per liter and hour (corresponding to 345U (L h)(-1)) has been determined in a high-density fed-batch process with a feed-forward exponential feeding strategy. During the fed-batch process, lactose was added intermittently to the culture. A final biomass concentration of 33 g L(-1) (based on cell dry weight) was obtained. Compared to shaking flask cultures in not optimized culture media, the overall volumetric P2O productivity has been improved by a factor of 110 using the fed-batch strategy and the optimized culture medium. Recombinant P2O was expressed in the cytoplasm with 9% of the total soluble protein being active P2O. In terms of physical and enzyme kinetic properties, the purified recombinant P2O was found to be similar to the previously published data of P2O isolated from its original host.     

Continuous cultivation of recombinant Escherichia coli: Existence of an optimum dilution rate for maximum plasmid and gene product concentration

Growth yield factors, plasmid stability, cellular plasmid content, and cloned gene product activity for Escherichia coli HB101 containing plasmid pDM246 were measured at several dilution rates in continuous culture. Cell mass yield per mass of glucose consumed declined with increasing dilution rate. There was no evidence of plasmid segregational instability in any experiments, none of which employed selective medium. Plasmid content per cell varied with population-specific growth rate as observed in earlier batch experiments with the same strain. Plasmid content declined with increasing specific growth rate following indication of a maximum number of plasmids per cell at specific growth rates of ca. 0.3 h(-1). Cloned gene product (beta-lactamase) activity exhibited a sharp maximum with respect to dilution rate in continuous culture. Qualitatively different results were observed in previous experiments in batch cultivation in which specific growth rate changes were effected by altering medium composition.     

Enhanced production of alpha-amylase in fed-batch cultures of Bacillus subtilis TN106[pAT5

Growth of Bacillus subtilis TN106[pAT5] and synthesis of plasmid-encoded protein (alpha-amylase) are investigated in batch, continuous, and fed-batch cultures using a defined medium containing glucose and/or starch as the carbohydrate source. The batch culture studies reveal that reduced availability of arginine hampers growth of recombinant cells (which lack an arginine synthesis gene) but promotes production of alpha-amylase and substitution of glucose by starch as the carbohydrate source leads to slower growth of recombinant cells and increased production of alpha-amylase per unit cell mass. Retention of recombinant cells over prolonged periods in continuous cultures is not possible without continuous application of antibiotic selection pressure owing to segregational plasmid instability. Fed-batch experiments with constant volumetric feed rate demonstrate that alpha-amylase production is enhanced at lower feed concentration of starch (sole carbohydrate source) and lower volumetric feed rate. Such slow addition of starch is however not conducive for growth of recombinant cells. The expression of the thermostable alpha-amylase gene carried on the recombinant plasmid pAT5 (derived from a plasmid isolated from a thermophilic bacterium) is promoted at higher temperatures, while growth of recombinant cells is depressed. In all batch and fed-batch experiments, production of alpha-amylase is observed to be inversely related to growth of recombinant cells. The efficacy of two-stage bioreactor operations, with growth of recombinant cells being promoted in the first stage and alpha-amylase production in the second stage, in attaining increased bulk alpha-amylase activity is demonstrated. (c) 1993 John Wiley & Sons, Inc.     

The study of heterogeneity of plasmid-bearing and plasmid-f ree populations of Bacillus subtilis under different environmental conditions

The population heterogeneity of recombinant and plasmid-free Bacillus subtilis strains introduced into aquatic microcosms was studied. After introduction, the population of the plasmid-free strain B. subtilis 2335 in microcosms has long been represented by both vegetative cells and spores, whereas, already ten days after introduction, the population of the recombinant strain B. subtilis 2335/105 (Km[symbol: see text]nf+) was represented only by spores. The number of plasmid copies in the spore isolates of the recombinant strain was the same as before introduction, but the plasmid abundance in the vegetative isolates of this strain decreased. The isolates of B. subtilis 2335/105 obtained from microcosms and the variants of this strain obtained by ten successive subcultures on M9 and 0.1 x M9 media with and without kanamycin (Km) differed in the number of plasmid copies, Km resistance, and maximum biomass yield during batch cultivation. Irrespective of the presence of Km, more than 50% of the variants subcultured on M9 medium showed reduced plasmid abundance. At the same time, about 70% of the variants subcultured on 0.1 x M9 medium with Km and 90% of the variants subcultured on the same medium without Km retained the initial number of plasmid copies. The variants subcultured on media with Km retained the initial biomass level. In more than 70% of the variants isolated from media without Km, the biomass yield increased.     

Optimization of cyclodextrin glycosyltransferase production from Klebsiella pneumoniae AS-22 in batch, fed-batch, and continuous cultures

Production of a novel cyclodextrin glycosyltransferase (CGTase) from Klebsiella pneumoniae AS-22 strain, which converts starch predominantly to alpha-CD at high conversion yields, in batch, fed-batch, and continuous cultures, is presented. In batch fermentations, optimization of different operating parameters such as temperature, pH, agitation speed, and carbon-source concentration resulted in more than 6-fold increase in CGTase activity. The enzyme production was further improved by two fed-batch approaches. First, using glucose-based feed to increase cell density, followed by starch-based feed to induce enzyme production, resulted in high cell density of 76 g dry cell weight/L, although the CGTase production was low. Using the second approach of a single dextrin-based feed, 20-fold higher CGTase was produced compared to that in batch fermentations with media containing tapioca starch. In continuous operation, more than 8-fold increase in volumetric CGTase productivity was obtained using dextrin-based media compared to that in batch culture using starch-based media.     

Kinetics of growth and ethanol production on different carbon substrates using genetically engineered xylose-fermenting yeast

Saccharomyces cerevisiae 424A (LNH-ST) strain was used for fermentation of glucose and xylose. Growth kinetics and ethanol productivity were calculated for batch fermentation on media containing different combinations of glucose and xylose to give a final sugar concentration of 20+/-0.8 g/L. Growth rates obtained in pure xylose-based medium were less than those for media containing pure glucose and glucose-xylose mixtures. A maximum specific growth rate micro(max) of 0.291 h(-1) was obtained in YPD medium containing 20 g/L glucose as compared to 0.206 h(-1) in YPX medium containing 20 g/L xylose. In media containing combinations of glucose and xylose, glucose was exhausted first followed by xylose. Ethanol production on pure xylose entered log phase during the 12-24h period as compared to the 4-10h for pure glucose based medium using 2% inoculum. When glucose was added to fermentation flasks which had been initiated on a pure xylose-based medium, the rate of xylose usage was reduced indicating cosubstrate inhibition of xylose consumption by glucose.     

Stringent regulation and high-level expression of heterologous genes in Escherichia coli using T7 system controllable by the araBAD promoter

The recombinant Eschreichia coli strain BL21 (BAD) was constructed to carry a chromosomal copy of T7 gene 1 fused to the araBAD promoter. To further characterize this expression system, strain BL21 (BAD) was transformed with the plasmid containing the carbamoylase gene from Agrobacterium radiobacter driven by the T7 promoter. Upon induction with L-arabinose, recombinant cells produced 100-fold increase in carbamoylase activity in comparison with uninduced cells on M9 semidefined medium plus glycerol. This protein yield accounts for 30% of total cell protein content. In addition, it was found that after 100 generations the plasmid harboring the carbamoylase gene remained firmly stable in strain BL21 (BAD), but its stability dropped to only 20-30% in strain BL21 (DE3), a commercial strain bearing T7 gene 1 regulated by the lacUV5 promoter in its chromosome. In an attempt to enhance the total protein yield, fed-batch fermentation process was carried out using a two-stage feeding strategy to compartmentalize cell growth and protein synthesis. In the batch fermentation stage, the culture was grown on glucose to reach the stationary growth phase. Subsequently, glycerol was fed to the culture broth and L-arabinose was augmented to induce protein production when cells entered the late log growth phase. As a result, a carbamoylase yield corresponding to 5525 units was obtained, which amounts to a 337-fold increase over that achieved on a shake-flask scale. Taken together, these results illustrate the practical usefulness of T7 system under control of the araBAD promoter for heterologous protein production.     

Large-scale production of endotoxin-free plasmids for transient expression in mammalian cell culture

Transient expression of recombinant proteins in mammalian cell culture in a 100-L scale requires a large quantity of plasmid that is very labour intensive to achieve with shake flask cultures and commercially available plasmid purification kits. In this paper we describe a process for plasmid production in 100-mg scale. The fermentation is carried out in a 4-L fed-batch culture with a minimal medium. The detection of the end of batch and triggering the exponential (0.1 h(-1)) feed profile was unattended and controlled by Multi-fermenter Control System. A restricted specific growth rate in fed-batch culture increased the specific plasmid yield compared to batch cultures with minimal and rich media. This together with high biomass concentration (68-107 g L(-1) wet weight) achieves high volumetric yields of plasmid (95-277 mg L(-1) depending on the construct). The purification process consisted of alkaline lysis, lysate clarification and ultrafiltration, two-phase extraction with Triton X-114 for endotoxin removal, anion-exchange chromatography as a polishing step, ultrafiltration and sterile filtration. Both fermentation and purification processes were used without optimisation for production of four plasmids yielding from 39 to 163 mg of plasmids with endotoxin content of 2.5 EU mg(-1) or less.     

Application of comparative proteome analysis to reveal influence of cultivation conditions on asymmetric bioreduction of β-keto ester by Saccharomyces cerevisiae

Industrial bakers' yeast strain Saccharomyces cerevisiae LH1 was selected for asymmetric reduction of ethyl benzoylacetate to (S)-ethyl 3-hydroxy-3-phenylpropionate. Higher reductive efficiency and higher cofactor availability were obtained with the alternation of cultivation condition (mainly growth medium). Compared to the bioreduction by yeast cells grown in malt extract (ME) medium, the concentration of substrate was increased 25-fold (up to 15.6 g/l) in the yeast peptone dextrose (YPD)-grown cells mediated bioreduction with 97.5% of enantioselective excess of (S)-product. The proteomic responses of S. cerevisiae LH1 cells to growth in aerobic batch cultures fed with either YPD or ME medium were examined and compared. Among the relative quantities of 550 protein spots in each gel, changes were shown in the expression level of 102 intracellular proteins when comparing YPD gel to ME gel. Most of the identified proteins were involved in energy metabolism and several cellular molecular biosynthetic pathway and catabolism. For YPD-grown yeast cells, not only enzymes involved in nicotinamide adenine dinucleotide phosphate regeneration, especially 6-phosphogluconate dehydrogenase, but also alcohol dehydrogenase 1 and D: -arabinose 1-dehydrogenase which had been demonstrated activity toward ethyl benzoylacetate to (S)-hydroxy ester were significantly upregulated. These changes provided us insight in the way the yeast cells adapted to a change in cultivation medium and regulated its catalytic efficiency in the bioreduction.     

Thermostability and xylan-hydrolyzing property of endoxylanase expressed in yeast Saccharomyces cerevisiae

The endoxylanase gene (xynB, GeneBank access code U51675), including its signal sequence, from Bacillus spp. was amplified and connected in frame downstream of yeast ADH1 promoter and then the resulting plasmid, pAEDX-1, was introduced into Saccharomyces cerevisiae. When the yeast transformants were grown on YPD medium, the majority of endoxylanase activity was detected in the extracellular culture medium, indicating that the signal peptide of Bacillus endoxylanase functioned well in yeast. In the batch cultivation of yeast transformants, the total expression level of endoxylanase and secretion efficiency were measured to be about 9.8 U/mL and 66.2%, respectively. The extracellular endoxylanase expressed in yeast showed an enhanced thermal stability due to the N-linked glycosylation. Through the hydrolysis of birchwood xylan with the endoxylanase, it was found that xylobiose and xylotriose were produced as major products with equimolar ratio.     

海水真菌定量分析方法的初步研究

为定量分析海水真菌,分别采用不同的采样方法采样;并采用5种培养基,每种培养基分别用4种不同的处理方式,共20种不同处理组合,筛选出适合定量分析海水中真菌的平板计数方案。结果表明,不同的采样方法下,真菌在同一培养基上的生长无显著性差异。在同一海水水样中,马铃薯培养基和马铃薯葡萄糖琼脂培养基用海水配制时几乎没有真菌生长;麦芽汁培养基在不同的处理条件下真菌略有生长,且各种处理间无明显差别,其种类主要是霉菌;察氏培养基和酵母菌浸出粉胨葡萄糖琼脂培养基在不同处理条件下真菌长势差别较大,种类主要是酵母菌。通过对20种培养组合的比较,选择酵母浸出粉胨葡萄糖琼脂培养基,用海水来配制培养基并用海水稀释样品的处理,可以培养出最大数量的海洋真菌。