Evaluation of Kluyveromyces marxianus FII 510700 grown on a lactose-based medium as a source of a natural bioemulsifier

Mannoprotein with emulsification properties was extracted from the cell walls of Kluyveromyces marxianus grown on a lactose-based medium by autoclaving cells in a citrate buffer at pH 7.The purified product was evaluated for chemical and physical stability to establish its potential use as a natural emulsifier in processed foods. The yield of purified bioemulsifier from this strain of K. marxianus was 4–7% of the original dry cell weight. The purified product, at a concentration of 12 g l^–1, formed emulsions that were stable for 3 months when subjected to a range of pH (3–11) and NaCl concentrations (2–50 g l^–1). The composition of this mannoprotein was 90% carbohydrate (mannan) and 4–6% protein. These values are similar to mannoprotein extracted from cells of Saccharomyces cerevisiae, which is the traditional source. Consequently K. marxianus cultivated on a low-cost lactose-based medium such as whey, a lactose-rich clean waste of the dairy industry, could be developed as a source of bioemulsifier for use in the food industry.     

Fed-batch fermentation for production of Kluyveromyces marxianusFII 510700 cultivated on a lactose-based medium

A strain of Kluyveromyces marxianus was grown in batch culture in lactose-based media at varying initial lactose concentrations (10–60 g L^–1) at 30°C, pH 5.0, dissolved oxygen concentrations greater than 20%. Increasing the concentration of mineral salts three-fold at 40 g L^–1 and 60 g L^–1 initial lactose concentration showed only a small increase in the yield of biomass, from 0.38 g g^–1 to 0.41 g g^–1, indicating that the initial batch cultures were not significantly nutrient- (mineral salts)-limited. A relatively high biomass concentration (105 g L^–1) was obtained in fed-batch culture following extended lactose feeding. An average specific growth rate (0.27 h^–1), biomass yield (0.38 g g^–1) and overall productivity (2.9 g L^–1 h^–1) were obtained for these fed-batch conditions. This fed-batch protocol provides a strategy for achieving relatively high concentrations and productivities of K. marxianus on other lactose-based substrate streams (e.g., whey) from the dairy industry.     

Microbial production of single-cell protein from deproteinized whey concentrates

Deproteinized sweet and sour cheese whey concentrates were investigated for their suitability as substrates for the production of single-cell protein with Kluyveromyces marxianus CBS 6556 up to a 100-l scale. An important factor for gaining high cell concentrations was the use of the Crabtree-negative strain K. marxianus CBS 6556. Supplements such as trace elements, ammonium and calcium were required for the complete conversion of sweet whey concentrates into biomass, whereas sour whey concentrates had to be supplemented with ammonium, trace elements and vitamins. After improvement, biomass dry concentrations of up to 50 g l⁻¹ could be reached with Yx/s values of 0.52 for sweet whey and of up to 65 g l⁻¹ with Yx/s values of 0.48 for sour whey concentrates. The chemical oxygen demand of the whey concentrates were reduced by 80%. The cells were used for the analysis of amino acid and ash composition, showing a distinct increase of eight out of ten essential amino acids compared to sweet and sour whey protein and exceeding the World Health Organisation guidelines for valine, leucine, isoleucine, threonine, phenylalanine and tyrosine.     

Metabolic engineering for direct lactose utilization by Saccharomyces cerevisiae

A recombinant strain of Saccharomyces cerevisiae, secreting -galactosidase from Kluyveromyces lactis, grew efficiently with more than 60 g lactose l^–1. The growth rate (0.23 h^–1) in a cheese-whey medium was close to the highest reported hitherto for other recombinant S. cerevisiae strains that express intracellular -galactosidase and lactose-permease genes. The conditions for growth and -galactosidase secretion in this medium were optimized in a series of factorial experiments. Best results were obtained at 23 °C for 72 h. Since the recombinant strain produced less than 3% ethanol from the lactose, it was also assayed for the production of fructose 1,6-bisphosphate from cheese whey, and 0.06 g l^–1 h^–1 were obtained.     

Screening of yeasts for the production of the aroma compound 2-phenylethanol in a molasses-based medium

Fourteen yeast strains were screened for production of 2-phenylethanol from l-phenylalanine with molasses as carbon source. Up to 1 g 2-phenylethanol l^–1 was obtained. Using oleyl alcohol as a second phase for in situ product removal to enhance the production of 2-phenylethanol increased the yield to about 3 g 2-phenylethanol l^–1 at 35 °C. The most productive strains were Kluyveromyces marxianus CBS 600 and CBS 397.     

The use of the replicating pDblet plasmid as a cloning vector with enhanced stability in Kluyveromyces marxianus

The replicating plasmid, pDblet, transformed the budding yeast Kluyveromyces marxianus to an efficiency of 10⁴ transformant g^–1 DNA. Transformed cells showed 1% of segregation rate without affecting their growth rate of 0.69 h^–1 and glucose consumption. These results were similar or better than the commonly used pE1 plasmid and suggests that pDblet can be used for cloning genes in K. marxianus.     

Utilization of protein-hydrolyzed cheese whey for production of β-galactosidase by Kluyveromyces marxianus

We studied the utilization of protein-hydrolyzed sweet cheese whey as a medium for the production of β-galactosidase by the yeasts Kluyveromyces marxianus CBS 712 and CBS 6556. The conditions for growth were determined in shake cultures. The best growth occurred at pH 5.5 and 37°C. Strain CBS 6556 grew in cheese whey in natura, while strain CBS 712 needed cheese whey supplemented with yeast extract. Each yeast was grown in a bioreactor under these conditions. The strains produced equivalent amounts of β-galactosidase. To optimize the process, strain CBS 6556 was grown in concentrated cheese whey, resulting in a higher β-galactosidase production. The β-galactosidase produced by strain CBS 6556 produced maximum activity at 37°C, and had low stability at room temperature (30°C) as well as at a storage temperature of 4°C. At −4°C and −18°C, the enzyme maintained its activity for over 9 weeks. Received 20 January 1999/ Accepted in revised form 30 April 1999     

Selection of yeast strains for lactose hydrolysis in dairy effluents

The ability of eight selected yeast strains growing in unsupplemented whey permeate to abate its lactose concentration has been studied. All strains reached 1 × 10⁸ colony forming units (cfu) ml⁻¹ by 20h of culture. Rates of lactose disappearance in permeate were poorly correlated with intracellular lactase levels. Maximal lactase activity levels were registered by Candida kefir NCYC 143 and Kluyveromyces marxianus NCYC 1548 cells, which reached 200 nmol ONP min⁻¹ 10⁻⁷ cells. Large fluctuations in enzymatic activity were observed during incubation, presumably as a result of the reciprocal effects between lactase activity and both galactose (0–1.9 mM) and lactose (0–143 mM) concentrations in the permeate.     

Thermotolerant single cell protein production byKluyveromyces marxianus var.marxianus

Summary Amino acid analyses were undertaken on single cell protein (SCP) produced by thermotolerant strains ofKluyveromyces marxianus var.marxianus grown on sugar cane molasses at 40°C. The maximum conversion of available sugars to biomass at 45°C was only 10.8% (g dry wt.·g^–1 total sugars). The amino acid composition of the SCP did not differ markedly from that reported for other yeast species.     

Production of S-adenosyl- L-methionine by a mutant strain of Kluyveromyces lactis

S-Adenosyl-l-methionine (AdoMet) was produced by a mutant strain Kluyveromyces lactis AM-65 grown on whey. A full factorial design method of three factors – (NH₄)₂SO₄ (factor x ₁), corn steep liquor (factor x ₂) and l-methionine (factor x ₃) on three levels – was used to determine the optimal medium conditions for the production of AdoMet. A time course shake-flask experiment in optimal whey medium (x ₁=3.1 g l^–1, x ₂=12.7 g l^–1, x ₃=4.6 g l^–1) was also carried out and the results confirmed the results of the factorial design and subsequent quadratic modelling and optimization of AdoMet production which reached 90 mg g^–1 cell dry wt.     

Continuous ethanol fermentation of cheese whey powder solution: effects of hydraulic residence time

Continuous ethanol fermentation of cheese whey powder solution was realized using pure culture of Kluyveromyces marxianus (DSMZ 7239) at hydraulic residence times (HRT) between 12.5 and 60 h. Sugar utilization, ethanol and biomass formation were investigated as functions of HRT. Effluent sugar concentration decreased, but percent sugar utilization, ethanol and biomass concentrations increased with HRT. Ethanol productivity was maximum (0.745 gE l⁻¹h⁻¹) at an HRT of 43.2 h where the biomass productivity was almost minimum (0.18 gX l⁻¹ h⁻¹). The ethanol yield coefficient was almost constant at 0.4 gE g⁻¹S up to HRT of 43.2 h and the growth yield coefficient was minimum at HRT of 43.2 h. Kinetic models were developed and the constants were determined by using the experimental data.     

Production of poly(3-hydroxybutyrate) from whey by cell recycle fed-batch culture of recombinant Escherichia coli

A new fermentation strategy using cell recycle membrane system was developed for the efficient production of poly(3-hydroxybutyrate) (PHB) from whey by recombinant Escherichia coli strain CGSC 4401 harboring the Alcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes. By cell recycle, fed-batch cultivation employing an external membrane module, the working volume of fermentation could be constantly maintained at 2.3 l. The final cell concentration, PHB concentration and PHB content of 194 g l^–1, 168 g l^–1 and 87%, respectively, were obtained in 36.5 h by the pH-stat cell recycle fed-batch culture using whey solution concentrated to contain 280 g lactose l^–1 as a feeding solution, resulting in a high productivity of 4.6 g PHB l^–1 h^–1.     

Characterization of the superoxide dismutase SOD1 gene of Kluyveromyces marxianus L3 and improved production of SOD activity

Superoxide dismutase (SOD) activity is one major defense line against oxidative stress for all of the aerobic organisms, and industrial production of this enzyme is highly demanded. The Cu/Zn superoxide dismutase gene (KmSOD1) of Kluyveromyces marxianus L3 was cloned and characterized. The deduced KmSod1p protein shares 86% and 71% of identity with Kluyveromyces lactis and Saccharomyces cerevisiae Sod1p, respectively. The characteristic motifs and the amino acid residues involved in coordinating copper and zinc and in enzymatic function were conserved. To the aim of developing a microbial production of Cu/Zn superoxide dismutase, we engineered the K. marxianus L3 strain with the multicopy plasmid YG-KmSOD1 harboring the KmSOD1 gene. The production of KmSOD1p in K. marxianus L3 and K. marxianus L3 (pYG-KmSOD1) in response to different compositions of the culture medium was evaluated. The highest specific activity (472 U_SOD mg_prot ⁻¹) and the highest volumetric yield (8.8 × 10⁵ U_SOD l⁻¹) were obtained by the recombinant strain overexpressing KmSOD1 in the presence of Cu²⁺ and Zn²⁺ supplements to the culture media. The best performing culture conditions were positively applied to a laboratory scale fed-batch process reaching a volumetric yield of 1.4 × 10⁶ U_SOD l⁻¹. Electronic supplementary material The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

The high fermentative metabolism of Kluyveromyces marxianus UFV-3 relies on the increased expression of key lactose metabolic enzymes

The aim of this work was to obtain insights about the factors that determine the lactose fermentative metabolism of Kluyveromyces marxianus UFV-3. K. marxianus UFV-3 and Kluyveromyces lactis JA6 were cultured in a minimal medium containing different lactose concentrations (ranging from 0.25 to 64 mmol l⁻¹) under aerobic and hypoxic conditions to evaluate their growth kinetics, gene expression and enzymatic activity. The increase in lactose concentration and the decrease in oxygen level favoured ethanol yield for both yeasts but in K. marxianus UFV-3 the effect was more pronounced. Under hypoxic conditions, the activities of β-galactosidase and pyruvate decarboxylase from K. marxianus UFV-3 were significantly higher than those in K. lactis JA6. The expression of the LAC4 (β-galactosidase), RAG6 (pyruvate decarboxylase), GAL7 (galactose-1-phosphate uridylyltransferase) and GAL10 (epimerase) genes in K. marxianus UFV-3 was higher under hypoxic conditions than under aerobic conditions. The high expression of genes of the Leloir pathway, LAC4 and RAG6, associated with the high activity of β-galactosidase and pyruvate decarboxylase contribute to the high fermentative flux in K. marxianus UFV-3. These data on the fermentative metabolism of K. marxianus UFV-3 will be useful for optimising the conversion of cheese whey lactose to ethanol.     

Production of a thermostable extracellular lipase by Kluyveromyces marxianus

Kluyveromyces marxianus was grown in submerged culture in a complex medium with several potential inducers of lipolytic activity (triacylglycerols, fatty acids). The highest extracellular lipolytic enzyme production (about 80 U ml^–1 in 3 d) was obtained when the medium was supplemented with 2 g urea l^–1 plus 5 g tributyrin l^–1. Addition of surfactants (1 g l^–1) did not improve production. The lipase had a high thermal stability in aqueous solution (73% residual activity after 9 d at 50 °C, 16 min half-life time at 100 °C). It was also stable at acidic pH and showed good tolerance to organic solvents (70% residual activity after 2 d in n-hexane of cyclohexane).     

Production of bioethanol from organic whey using <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis>

Ethanol production by K. marxianus in whey from organic cheese production was examined in batch and continuous mode. The results showed that no pasteurization or freezing of the whey was necessary and that K. marxianus was able to compete with the lactic acid bacteria added during cheese production. The results also showed that, even though some lactic acid fermentation had taken place prior to ethanol fermentation, K. marxianus was able to take over and produce ethanol from the remaining lactose, since a significant amount of lactic acid was not produced (1–2 g/l). Batch fermentations showed high ethanol yield (~0.50 g ethanol/g lactose) at both 30°C and 40°C using low pH (4.5) or no pH control. Continuous fermentation of nonsterilized whey was performed using Ca-alginate-immobilized K. marxianus. High ethanol productivity (2.5–4.5 g/l/h) was achieved at dilution rate of 0.2/h, and it was concluded that K. marxianus is very suitable for industrial ethanol production from whey.     

Aroma compounds produced by Kluyveromyces marxianus in solid state fermentation on a packed bed column bioreactor

Studies were carried out for the production of aroma compounds by Kluyveromyces marxianus grown on cassava bagasse in solid state fermentation using packed bed reactors, testing two different aeration rates. Respirometric analysis was used to follow the growth of the culture. Headspace analysis of the culture by gas chromatography showed the production of 11 compounds, out of which nine were identified. Ethyl acetate, ethanol and acetaldehyde were the major compounds produced. Lower aeration rate (0.06l h^–1 g^–1 of initial dry matter) increased total volatile (TV) production and the rate of production was also increased at this aeration rate. Using an aeration rate of 0.06l h^–1 g^–1 maximum TV concentrations were reached at 24 h and at 40 h with 0.12l h^–1 g^–1.     

Pediocin production by recombinant lactic acid bacteria

Production of the anti-listerial bacteriocin, pediocin, by lactic acid bacteria (LAB) transformed with the cloning vector pPC418 (Ped⁺, 9.1 kb) was influenced by composition of media and incubation temperature. Maximum pediocin production, tested against Listeria innocua, by electrotransformants of Lactococcus lactis ssp. lactis was measured in tryptone/lactose/yeast extract medium after 24 h growth at 30 °C, while incubation at 40 °C was optimum for Ped⁺ transformants of Streptococcus thermophilus and Enterococcus faecalis. The amount of pediocin produced by S. thermophilus in skim milk and cheese whey supplemented with 0.5% yeast extract was estimated as 51000 units ml^–1 and 25000 units ml^–1, respectively. Pediocin production remained essentially unchanged in reconstituted skim milk or whey media diluted up to 10-fold. The results demonstrate the capacity of recombinant strains of LAB to produce pediocin in a variety of growth media including skim milk and inexpensive cheese whey-based media, requiring minimum nutritional supplementation.     

High-Level Production of Heterologous Protein by Engineered Yeasts Grown in Cottage Cheese Whey

Cottage cheese whey is a cheese industry by-product still rich in proteins and lactose. Its recycling is seldom cost-effective. In this work we show that the lactose-utilizing yeast Kluyveromyces lactis, engineered for production of recombinant human lysozyme, can be grown in cottage cheese whey, resulting in high-level production of the heterologous protein (125 μg/ml).     

Hydrolysis of whey lactose using CTAB-permeabilized yeast cells

Disposal of lactose in whey and whey permeates is one of the most significant problems with regard to economics and environmental impact faced by the dairy industries. The enzymatic hydrolysis of whey lactose to glucose and galactose by β-galactosidase constitutes the basis of the most biotechnological processes currently developed to exploit the sugar content of whey. Keeping this in view, lactose hydrolysis in whey was performed using CTAB permeabilized Kluyveromyces marxianus cells. Permeabilization of K. marxianus cells in relation to β-galactosidase activity was carried out using cetyltrimethyl ammonium bromide (CTAB) to avoid the problem of enzyme extraction. Different process parameters (biomass load, pH, temperature, and incubation time) were optimized to enhance the lactose hydrolysis in whey. Maximum hydrolysis (90.5%) of whey lactose was observed with 200 mg DW yeast biomass after 90 min of incubation period at optimum pH of 6.5 and temperature of 40 °C.