Formation of ethyl acetate by Kluyveromyces marxianus on whey during aerobic batch and chemostat cultivation at iron limitation

The ability of Kluyveromyces marxianus to convert lactose into ethyl acetate offers a chance for an economic reuse of whey. Former experiments with K. marxianus DSM 5422 proved limitation of growth by iron (Fe) or copper as a precondition for significant ester synthesis. Several aerobic batch and chemostat cultivations were done with whey-borne media of a variable Fe content for exploring the effect of Fe on growth, the Fe content of biomass, and metabolite synthesis. At low Fe doses, Fe was the growth-limiting factor, the available Fe was completely absorbed by the yeasts, and the biomass formation linearly depended on the Fe dose governed by a minimum Fe content in the yeasts, x _Fe,min. At batch conditions, x _Fe,min was 8.8???g/g, while during chemostat cultivation at D?=?0.15?h^?1, it was 23???g/g. At high Fe doses, sugar was the growth-limiting factor, Fe was more or less absorbed, and the formed biomass became constant. Significant amounts of ethyl acetate were only formed at Fe limitation while high Fe doses suppressed ester formation. Analysis of formed metabolites such as glycerol, pyruvate, acetate, ethanol, ethyl acetate, isocitrate, 2-oxoglutarate, succinate, and malate during chemostat cultivation allowed some interpretation of the Fe-dependent mechanism of ester synthesis; formation of ethyl acetate from acetyl-SCoA and ethanol is obviously initiated by a diminished metabolic flux of acetyl-SCoA into the citrate cycle and by a limited oxidation of NADH in the respiratory chain since Fe is required for the function of aconitase, succinate dehydrogenase, and the electron-transferring proteins.     

Utilisation of cheese whey as an alternative growth medium for recombinant strains of Kluyveromyces marxianus

Kluyveromyces marxianus KMDB-1, a plasmid-bearing recombinant, not carrying any particular gene of relevance, derived from auxotrophic strain KMS-2 (ura ^–), grew in cheese whey with a maximum specific growth rate of 0.34 h^–1. This recombinant strain showed the same lactose uptake and extracellular protease production kinetics as the wild type CBS6556 with no evidence of catabolite repression. The plasmid was retained in 50% of cells after 36 h of batch culture. The presence of this vector in Kluyveromyces marxianus, which possesses no natural plasmids, together with the absence of any metabolic loading effect, creates a suitable microbial system for cheese whey processing for potential value-added product formation.     

Oligosaccharides extracted from cell walls of Kluyveromyces marxianus grown on whey

After whey fermentation by Kluyveromyces marxianus var. marxianus (30°C, pH 4.5, 24 h) and autolysis of the cells (50°C, pH 6.5, 12 h), the subsequent extracts were centrifuged (10,000 × g, 4°C, 15 min), and the cell walls were separated from the autolysates. Cell walls were then treated with: (i) 0.75M NaOH (75°C, 20 h) ; or (ii) lytic enzymes, 0.0025–5.0% (w/v), in 5 mM phosphate buffer (pH 6.5–7.0) (40°C, 24 h). The lytic enzymes were denaturated (80°C, 15 min), and the alkali solutions were neutralized with 0.5M acetic acid, before centrifugation. The supernatants were concentrated by a Speed-Vac concentrator, and analyzed by HPLC, equipped with a TSK-Amide 80 column (1.0 ml/ min of water/acetonitrile, 35/65 ratio, 60°C, 40 min). Tetrasaccharides were detected. Gels were formed when cell walls were treated with NaOH. © Rapid Science Ltd. 1998     

Simplified feeding strategies for fed-batch cultivation of Kluyveromyces marxianus in cheese whey

The present work reports the effect of simple feeding strategies to obtain high-cell-density cultures of Kluyveromyces marxianus maximizing β-galactosidase productivity using cheese whey as basic medium. Linear and exponential feeding strategies, with feeding times of 20, 25 and 35 h, and three different feeding media concentrations (140 g/L, 210 g/L, and 280 g/L lactose concentration), were tested. Final biomass concentration reached 35 g cells dry weight/L and our results showed that continuous lactose addition to culture were able to produce high specific enzyme activities, consequently improving volumetric activities of β-galactosidase when compared to batch cultivations. The best fed-batch strategy, which was the feeding of three-fold lactose concentration in the cheese whey-medium during 25 h, resulted in β-galactosidase productivity of 291 U/L h, representing an increase of more than 50% compared to batch cultivations.     

Fed-batch fermentation to produce oligonucleotides from Kluyveromyces marxianus grown on whey

Oligonucleotides (ON) extracted from yeasts are used as antiviral agents, immunostimulators, and flavour enhancers. Fed-batch fermentation of cheese whey by Kluyveromyces marxianus was carried out to produce high biomass yields to extract ON. K marxianus was grown for 20 h in medium containing 5% (w/v) dehydrated whey, at 30°C (pH 4.5), with agitation (350 rpm), and under aeration (1.0–2.0 vvm). After 20 h, media containing 10–15% (w/v) of dehydrated whey were added at different flow rates (180–230 ml/h). Samples were analyzed at 6–8 h intervals for cell count, lactose consumption, and ethanol production. Maximum production of biomass (28.13 g/l), yield (0.58 g/g), productivity (2.42 g/l per h), and specific growth rate (0.63 1/h) were obtained when medium containing 15% (w/v) of whey was added at 180 ml/h under 2 vvm aeration. Fed-batch fermentation converted 95% of whey lactose into biomass.     

Identification of volatile flavour compounds obtained in culture of Kluyveromyces marxianus

When Kluyveromyces marxianus was cultivated on a defined medium, flavour volatile compounds accumulated in the broth. Besides superior alcohols and aldehydes, acids and fruit esters could be analyzed by gas chromatography and coupled gas chromatography-mass spectrometry. The predominant components are isoamyl alcohol, 2-phenylethyl alcohol and isobutyric acid with 180 mg/L, 400 mg/L and 290 mg/L broth, respectively.     

Effects of glucose supply on myeloma growth and metabolism in chemostat culture

The effects of the glucose supply on growth and metabolism of an SP2/0 derived recombinant myeloma cell line were studied in chemostat culture during growth on IMDM medium at a fixed dilution rate of 0.032 h^?1. Lowering of the feed medium glucose concentration from 25.0 to 1.4 mmol/L resulted in a decrease of steady-state viable cell concentration from 1.9 × 10⁹ L^?1, whereas viability remained above 90%. Mass balances indicated that only a minor amount of glucose was utilized via the TCA cycle irrespective of the glucose concentration in the feed medium. The apparent biosynthetic yield of cells from ATP was independent of the ratio between the specific glucose and glutamine consumption rate. It is concluded that the primary role of glucose is the provision of intermediates for anabolic reactions. In addition, glucose may play an indirect catabolic role in the process of glutaminolysis by providing the pyruvate for the transamination of glutamate to alanine and α-ketoglutarate. At low glucose concentrations in the feed medium, glutamine is probably the sole energy source for this myeloma in chemostat culture. © 1995 Wiley-Liss, Inc.     

Evolutionary adaptation of Kluyveromyces marxianus strain for efficient conversion of whey lactose to bioethanol

The aim of the present work is to develop an osmotolerant yeast strain with high lactose utilization and further use it to ferment lactose rich whey permeate for high ethanol titer and to reduce energy consumption. Ethanol production and growth rate of selected MTCC 1389 strain were quite high in whey containing lactose up to 150 g/L but it remains constant in lactose concentration (200 g/L) as cells encountered osmotic stress. Thus, strain MTCC 1389 was used for an adaptation to lactose concentration 200 g/L for 65 days and used further for fermentation of lactose rich whey. Fermentation with an adapted K. marxianus MTCC 1389 strain in laboratory fermenter resulted in ethanol titer of 79.33 g/L which is nearly 17.5% higher than the parental strain (66.75 g/L). Expression analysis of GPD1, TPS1and TPS2 found upregulated in lactose adapted K. marxianus strain as compared to the parental strain. These results suggest that an adapted K. marxianus strain accumulates glycerol and trehalose in response to lactose stress and improve osmotolerance in K. marxianus cells. Thus, the study illustrates that evolutionary engineering is an efficient strategy to obtain a superior biofuel yeast strain, which efficiently ferments four-fold concentrated cheese whey.     

Use of chemostat data for modelling extracellular-inulinase production by Kluyveromyces marxianus in a high-cell-density fed-batch process

Production of extracellular inulinase by low-cell-density (2 kg dry weight·m⁻³) sucrose-limited chemostat cultures of Kluyveromyces marxianus obeyed saturated kinetics at dilution rates ranging from 0.02 to 0.5 h⁻¹. A non-structured Monod-type equation, describing the relation between specific growth rate and specific extracellular-inulinase production rate, was used to fit experimental data. THis equation was subsequently incorporated in a model for the production of biomass and extracellular inulinase in a high-cell-density (> 100 kg dry weight·m⁻³) fed-batchculture of K. marxianus grown on sucrose. The model adequately described biomass production in the fed-batch culture. However, the production of extracellular inulinase in the fed-batch process was slightly higher than predicted by the model. This observation may be related to differences in growth conditions between in the chemostat and fed-batch cultures.     

Production of inulinase by mixed culture of Aspergillus niger and Kluyveromyces marxianus

Summary Inulinase activity produced by a mixed culture of Aspergillus niger and Kluyveromyces marxianus growing on Jerusalem artichoke powder was investigated. Inulinase produced by this mixed culture had a higher invertase-type activity than inulinase from respective monocultures. When hydrolysis was carried out at 50°C with Jerusalem artichoke exctract (total sugar 16% w/v) at pH 5.0, 90% hydrolysis was achieved after 4 h with 5% v/v of crude cell free enzyme preparation.     

Improved ethanol production from whey with Saccharomyces cerevisiae using permeabilized cells of Kluyveromyces marxianus

Permeabilized cells of Kluyveromyces marxianus CCY eSY2 were tested as the source of lactase in the ethanol fermentation of concentrated deproteinized whey (65–70 g/l lactose) by Saccharomyces cerevisiae CCY 10–13–14. Rapid lactose hydrolysis by small amounts of permeabilized cells following the fermentation of released glucose and galactose by S. cerevisiae resulted in a twofold enhancement of the overall volumetric productivity (1.03 g/l × h), compared to the fermentation in which the lactose was directly fermented by K. marxianus.     

Formation of ethyl acetate by Kluyveromyces marxianus on whey: Influence of aeration and inhibition of yeast growth by ethyl acetate

The ability of the yeast Kluyveromyces marxianus to convert lactose into ethyl acetate offers good opportunities for the economical reuse of whey. The formation of ethyl acetate as a bulk product depends on aerobic conditions. Aeration of the bioreactor results in discharge of the volatile ester with the exhaust gas that allows its process‐integrated recovery. The influence of aeration (varied from 10 to 50 L/h) was investigated during batch cultivation of K. marxianus DSM 5422 in 0.6 L whey‐borne medium using a stirred reactor. With lower aeration rates, the ester accumulated in the bioreactor and reached higher concentrations in the culture medium and the off gas. A high ester concentration in the gas phase is considered beneficial for ester recovery from the gas, while a high ester concentration in the medium inhibited yeast growth and slowed down the process. To further investigate this effect, the inhibition of growth by ethyl acetate was studied in a sealed cultivation system. Here, increasing ester concentrations caused a nearly linear decrease of the growth rate with complete inhibition at concentrations greater than 17 g/L ethyl acetate. Both the cultivation process and the growth rate depending on ethyl acetate were described by mathematical models. The simulated processes agreed well with the measured data.     

Formation of ethyl acetate by Kluyveromyces marxianus on whey: studies of the ester stripping

Kluyveromyces marxianus is capable of converting lactose into ethyl acetate offering a chance for an economical reuse of whey. The microbial formation of ethyl acetate as a bulk product calls for an aerobic process and, thus, the highly volatile ethyl acetate is discharged from the aerated bioreactor. This stripping process was modeled and investigated experimentally. The stripping rate was proportional to the gas flow and nearly independent of the stirring rate since the stripping was governed by the absorption capacity of the exhaust gas rather than the phase transfer. Cooling the exhaust gas did not noticeably influence the stripping. One batch experiment is presented in detail to demonstrate the formation of ethyl acetate by K. maxianus DSM 5422 on whey. Further batch experiments showed that a substantial formation of ethyl acetate only occurred when the yeast growth was limited by a lack of trace elements. The highest product yield observed was 0.25 g ethyl acetate per g lactose which is nearly 50% of the theoretical maximum.     

Protoplast transformation of Kluyveromyces marxianus

The dairy yeast Kluyveromyces marxianus is a promising cell factory for producing bioethanol and heterologous proteins, as well as a robust synthetic biology platform host, due to its safe status and beneficial traits, including fast growth and thermotolerance. However, the lack of high-efficiency transformation methods hampers the fundamental research and industrial application of this yeast. Protoplast transformation is one of the most commonly used fungal transformation methods, but it yet remains unexplored in K. marxianus. Here, we established the protoplast transformation method of K. marxianus for the first time. A series of parameters on the transformation efficiency were optimized: cells were collected in the late-log phase and treated with zymolyase for protoplasting; the transformation was performed at 0 °C with carrier DNA, CaCl₂, and PEG; after transformation, protoplasts were recovered in a solid regeneration medium containing 3–4% agar and 0.8 m sorbitol. By using the optimized method, plasmids of 10, 24, and 58 kb were successfully transformed into K. marxianus. The highest efficiency reached 1.8 × 10⁴ transformants per μg DNA, which is 18-fold higher than the lithium acetate method. This protoplast transformation method will promote the genetic engineering of K. marxianus that requires high-efficiency transformation or the introduction of large DNA fragments.     

Effects of glutamine supply on growth and metabolism of mammalian cells in chemostat culture

Glutamine is a major source of energy, carbon, and nitrogen for mammalian cells. The amount of glutamine present in commercial mammalian cell media is, however, not necessarily balanced with cell requirements. Therefore, the effects of glutamine limitation on the physiology of two mammalian cell lines were studied in steady-state chemostat cultures fed with IMDM medium with 5% serum. The cell lines used were MN12, a mouse-mouse hybridoma, and SP2/0-Ag14, a mouse myeloma often used in hybridoma fusions. Cultures, grown at a fixed dilution rate of 0.03 h(-1), were fed with media containing glutamine concentrations ranging from 0.5 to 4 mmol L(-1). Biomass dry weight and cell number were linearly proportional to the glutamine concentrations fed, between 0.5 and 2 mmol L(-1), and glutamine was completely consumed by both cell lines. From this it was concluded that glutamine was the growth-limiting substrate in this concentration range and that the standard formulation of IMDM medium contains a twofold excess of glutamine. In glutamine-limited cultures, the specific rates of ammonia and alanine production were low compared to glutamine-excess cultures containing 4 mmol L(-1) glutamine in the feed medium. The specific consumption rates of nearly all amino acids decreased with increasing glutamine feed, indicating that, in their metabolic function, they may partially be replaced by glutamine. Both cell lines reacted similarly to differences in glutamine feeding in all aspects investigated, except for glucose metabolism, In SP2/0-Ag14 glutamine feed concentrations did not affect the specific glucose consumption, whereas in MN12 this parameter increased with increasing amounts of glutamine fed. This systematic study using controlled culture conditions together with a detailed analysis of culture data shows that, although cells may react similarly in many aspects, cell-line-specific characteristics may be encountered even with respect to fundamental physiological responses like the interaction of the glutamine and glucose metabolism. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 272-286, 1997.     

Physiology of the yeast Kluyveromyces marxianus during batch and chemostat cultures with glucose as the sole carbon source

Growth, substrate consumption, metabolite formation, biomass composition and respiratory parameters of Kluyveromyces marxianus ATCC 26548 were determined during aerobic batch and chemostat cultivations, using mineral medium with glucose as the sole carbon source, at 30 degrees C and pH 5.0. Carbon balances closed within 95-101% in all experiments. A maximum specific growth rate of 0.56 h(-1), a biomass yield on glucose of 0.51 g g(-1), and a maximum specific consumption of oxygen of 11.1 mmol g(-1) h(-1) were obtained during batch cultures. The concentration of excreted metabolites was very low at the culture conditions applied, representing 6% of the consumed carbon at most. Acetate and pyruvate were excreted to a larger extent than ethanol under the batch conditions, and the protein content accounted for 54.6% of the biomass dry weight. Steady states were obtained during chemostats at dilution rates of 0.1, 0.25 and 0.5 h(-1). At the two former dilution rates, cells grew at carbon limitation and the biomass yield on glucose was similar to that obtained under the batch conditions. Metabolite formation was rather low, accounting for a total of 0.005 C-mol C-mol(-1) substrate. At 0.5 h(-1), although the biomass yield on glucose was similar to the value obtained under the above-mentioned conditions, the cultivation was not under carbon limitation. Under this condition, 2-oxoglutarate, acetate, pyruvate and ethanol were the prevalent metabolites excreted. Total metabolite formation only accounted to 0.056 C-mol C-mol(-1) of substrate. A very high protein and a low carbohydrate content (71.9% and 9.6% of biomass dry weight, respectively) were measured in cells under this condition. It is concluded that K. marxianus aligns with the so-called aerobic-respiring or Crabtree-negative yeasts. Furthermore, it has one of the highest growth rates among yeasts, and a high capacity of converting sugar into biomass, even when carbon is not the limiting nutrient. These results provide useful data regarding the future application of K. marxianus in processes aimed at the production of biomass-linked compounds, with high yields and productivities.