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.     

Formation of ethyl acetate by Kluyveromyces marxianus on whey during aerobic batch cultivation at specific trace element limitation

Kluyveromyces marxianus is able to transform lactose into ethyl acetate as a bulk product which offers a chance for an economical reuse of whey-borne sugar. Ethyl acetate is highly volatile and allows its process-integrated recovery by stripping from the aerated bioreactor. Extensive formation of ethyl acetate by K. marxianus DSM 5422 required restriction of yeast growth by a lack of trace elements. Several aerobic batch processes were done in a 1-L stirred reactor using whey-borne culture medium supplemented with an individual trace element solution excluding Mn, Mo, Fe, Cu, or Zn for identifying the trace element(s) crucial for the observed ester synthesis. Only a lack of Fe, Cu, or Zn restricted yeast growth while exclusion of Mn and Mo did not exhibit any effect due to a higher amount of the latter in the used whey. Limitation of growth by Fe or Cu caused significant production of ethyl acetate while limitation by Zn resulted in formation of ethanol. A lack of Fe or Cu obviously makes the respiratory chain inefficient resulting in an increased mitochondrial NADH level followed by a reduced metabolic flux of acetyl-SCoA into the citrate cycle. Synthesis of ethyl acetate from acetyl-SCoA and ethanol by alcoholysis is thus interpreted as an overflow metabolism.     

Growth of Kluyveromyces marxianus and formation of ethyl acetate depending on temperature

Conversion of lactose into ethyl acetate by Kluyveromyces marxianus allows economic reuse of whey-borne sugar. The high volatility of ethyl acetate enables its process-integrated recovery by stripping. This stripping is governed by both the aeration rate and the partition coefficient, K _EA,L/G. Cultivation at elevated temperatures should decrease the K _EA,L/G value and thus favor stripping. K. marxianus DSM 5422 as a potent producer of ethyl acetate was cultivated aerobically in whey-borne media for studying temperature-dependent growth and ester formation. Shake flask cultivation proved thermal tolerance of this yeast growing from 7 to 47 °C with a maximum rate of 0.75 h^?1 at 40 °C. The biomass yield was 0.41 g/g at moderate temperatures while low and high temperatures caused distinct drops. The observed μ-T and Y _X/S-T dependencies were described by mathematical models. Further cultivations were done in an 1-L stirred reactor for exploring the effect of temperature on ester synthesis. Cultivation at 32 °C caused significant ester formation (Y _EA/S?=?0.197 g/g) while cultivation at 42 °C suppressed ester synthesis (Y _EA/S?=?0.002 g/g). The high temperature affected metal dissolution from the bioreactor delivering iron for yeast growth and preventing ester synthesis. Cultivation at 32 °C with a switch to 42 °C at the onset of ester synthesis allowed quick and efficient ester production (Y _EA/S?=?0.289 g/g). The high temperature lowered the K _EA,L/G value from 78 to 44 L/L which heightened the gas-phase ester concentration (favoring ester recovery) without increasing the liquid-phase concentration (avoiding product inhibition).     

Production of ethyl acetate from dilute ethanol solutions by Candida utilis

The conversion of ethanol to ethyl acetate has an advantage as a method of ethanol recovery since ethyl acetate is amenable to simple solvent extraction. The potential of Candida utilis in this conversion was studied. The kinetics of accumulation of ethanol and ethyl acetate in glucose-grown C. utilis showed that ester formation resulted from ethanol utilization under appropriate aeration and was inhibited by Fe(3+) supplementation. Candida utilis converted ethanol to ethyl acetate optimally at pH 5.0-7.0. The five-hour rate of ester production increased as the ethanol concentration increased to 10 g/L, and rapidly declined to zero at concentrations exceeding 35 g/L. Thus, C. utilis has potential to recover dilute ethanol in the form of ethyl acetate.     

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.     

High throughput,colorimetric screening of microbial ester biosynthesis reveals high ethyl acetate production from Kluyveromyces marxianus on C5, C6, and C12 carbon sources

Advances in genome and metabolic pathway engineering have enabled large combinatorial libraries of mutant microbial hosts for chemical biosynthesis. Despite these advances, strain development is often limited by the lack of high throughput functional assays for effective library screening. Recent synthetic biology efforts have engineered microbes that synthesize acetyl and acyl esters and many yeasts naturally produce esters to significant titers. Short and medium chain volatile esters have value as fragrance and flavor compounds, while long chain acyl esters are potential replacements for diesel fuel. Here, we developed a biotechnology method for the rapid screening of microbial ester biosynthesis. Using a colorimetric reaction scheme, esters extracted from fermentation broth were quantitatively converted to a ferric hydroxamate complex with strong absorbance at 520 nm. The assay was validated for ethyl acetate, ethyl butyrate, isoamyl acetate, ethyl hexanoate, and ethyl octanoate, and achieved a z‐factor of 0.77. Screening of ethyl acetate production from a combinatorial library of four Kluyveromyces marxianus strains on seven carbon sources revealed ethyl acetate biosynthesis from C5, C6, and C12 sugars. This newly adapted method rapidly identified novel properties of K. marxianus metabolism and promises to advance high throughput microbial strain engineering for ester biosynthesis.     

Continous ethyl acetate production by Kluyveromyces fragilis on whey permeate

The synthesis of ethyl acetate by Kluyveromyces fragilis on diluted whey permeate was studied. Ethanol, lactose and O₂ are the direct precursors for ethyl acetate synthesis by this yeast. Ethyl acetate production is affected by many parameters, particularly the carbon/nitrogen (C/N) ratio, Tween 80 and iron. Ethyl acetate synthesis is optimum for C/N = 45. Tween 80 lowered slightly the level of ethyl acetate whereas iron completely stopped ethyl acetate production. The level of ethanol in the feed, the dissolved O₂ (DO) and dilution rate (D) were also optimised. Thus at D = 0.24 h ^–1, for 4 g/l of ethanol in the feed and 40% DO, the productivity of ethyl acetate was optimal (0.7 g/l per hour). Correspondence to: A. Miclo     

Acetic acid removal from corn stover hydrolysate using ethyl acetate and the impact on Saccharomyces cerevisiae bioethanol fermentation

Acetic acid is introduced into cellulose conversion processes as a consequence of composition of lignocellulose feedstocks, causing significant inhibition of adapted, genetically modified and wild‐type S. cerevisiae in bioethanol fermentation. While adaptation or modification of yeast may reduce inhibition, the most effective approach is to remove the acetic acid prior to fermentation. This work addresses liquid–liquid extraction of acetic acid from biomass hydrolysate through a pathway that mitigates acetic acid inhibition while avoiding the negative effects of the extractant, which itself may exhibit inhibition. Candidate solvents were selected using simulation results from Aspen Plus?, based on their ability to extract acetic acid which was confirmed by experimentation. All solvents showed varying degrees of toxicity toward yeast, but the relative volatility of ethyl acetate enabled its use as simple vacuum evaporation could reduce small concentrations of aqueous ethyl acetate to minimally inhibitory levels. The toxicity threshold of ethyl acetate, in the presence of acetic acid, was found to be 10 g L^?1. The fermentation was enhanced by extracting 90% of the acetic acid using ethyl acetate, followed by vacuum evaporation to remove 88% removal of residual ethyl acetate along with 10% of the broth. NRRL Y‐1546 yeast was used to demonstrate a 13% increase in concentration, 14% in ethanol specific production rate, and 11% ethanol yield. This study demonstrated that extraction of acetic acid with ethyl acetate followed by evaporative removal of ethyl acetate from the raffinate phase has potential to significantly enhance ethanol fermentation in a corn stover bioethanol facility. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:929–937, 2016     

Mechanism of ethyl acetate synthesis by Kluyveromyces fragilis

Abstract The enzymes implicated in ethyl acetate synthesis and the catabolism of ethanol by Kluyveromyces fragilis were investigated under varying growth conditions. The culture was grown continuously to D = 0.25 h⁻¹ on diluted whey permeate. The results showed that ethyl acetate synthesis by Kluyveromyces fragilis is catalysed by both an esterase and an alcohol acetyltransferase. The esterase is a constitutive enzyme, while alcohol acetyltransferase is inducible. The catabolism of ethanol by Kluyveromyces fragilis resulted in production of ethyl acetate, acetate and acetaldehyde. The glyoxylic shunt is totally inactive in these conditions. The production of acetaldehyde is only governed by an alcohol dehydrogenase.     

Effect of iron and EDTA on ethyl acetate accumulation in Candida utilis

Summary Production of economically-recoverable products from dilute sugar or ethanol is of practical importance. Conversion of glucose to ethyl acetate by Candida utilis was inhibited by FeCl₃ supplementation as low as 10 uM. EDTA added at the onset of growth on glucose relieved such an inhibition and also caused faster and greater amounts of accumulation of the ester. Addition of EDTA during conversion of ethanol to ethyl acetate showed little effect. EDTA may affect cell permeability and/or oxidative metabolism. For continual ethyl acetate production iron limitation must be maintained during as well as before ethanol utilization.EDTA = Ethylenediaminetetraacetic acid.     

Gas phase ethyl acetate production in a batch bioreactor

Gas phase ethyl acetate production was studied using a porcine pancreatic lipase powder. It was observed that gaseous ethyl acetate was produced from gaseous ethanol and acetic acid. Accordingly, the effects of amount of lipase powder, gaseous ethanol and acetic acid concentrations, and reaction temperature on the performance of a batch bioreactor were investigated. Apparent Michaelis-Menten constant of ethanol was 0.163 [μM] and there was no inhibition by ethanol over the range investigated. As acetic acid concentration increased, ethyl acetate production increased to a maximum, then decreased, thus suggesting the inhibition effects by acetic acid. Over the reaction temperature of 25–55?°C, activation energy was calculated as 3.93 kcal/gmol and initial reaction rate was obtained as follows: r?=?75.7 exp(?1975.7/T) [μM/mg of lipase/hr]     

Experimental design and metabolic flux analysis tools to optimize industrially relevant Haemophilus influenzae type b growth medium

Haemophilus influenzae type b (Hib), a Gram‐negative capsulated bacterium, is a causative agent of meningitis worldwide. The capsular polysaccharide, a high molecular mass polymer consisting of the repeated units of the polyribosyl‐ribitol‐phosphate, is considered the main virulence factor and it is used as an antigen to vaccines, conjugated to a carrier protein. The industrial production of the polysaccharide requires the cultivation of Hib in rich medium, which impacts process costs and product recovery. In this study, a central composite rotational experimental design strategy was used to access the influence of key components of culture medium (soy peptone, yeast extract and glucose) on biomass formation and polysaccharide production in shake‐flasks. The optimized medium formulation, containing half of the usual yeast extract and soytone concentrations, was further validated in batch bioreactor cultivations. High polysaccharide production (～500 mg/L) was obtained in a cheaper and more competitive production process for use in Hib vaccine production. In addition, simulations of a metabolic model describing Hib central metabolism were used to assess the role of key amino acids on growth. A chemically defined medium supplemented only with amino acids from α‐ketoglutarate and oxaloacetate families as well as phenylalanine was suggested as a promising alternative for reduced acetate accumulation and enhanced polysaccharide production in Hib cultures. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1508–1519, 2017     

Influence of glucose and oxygen on the production of ethyl acetate and isoamyl acetate by a <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> strain during alcoholic fermentation

The effect of glucose and dissolved oxygen in a synthetic medium simulating the standard composition of grape juice on the production of ethyl acetate and isoamyl acetate by a Saccharomyces cerevisiae strain during alcoholic fermentation was studied. The specific in vitro activity of alcohol acetyltransferase (AATase, EC 2.3.1.84) and esterases (ESase, EC 3.1.1.1; hydrolysis and synthesis of esters) in cell-free extracts was also examined. The specific activity of AATase for ethyl acetate was found to peak at the beginning of the exponential growth phase and that for isoamyl acetate at its end. While the glucose concentration only affected the maximum specific activity of AATase, and only slightly, oxygen inhibited such activity, to a greater extent for isoamyl acetate than for ethyl acetate. On the other hand, esterases were found to catalyse the synthesis of ethyl acetate only at a low or medium glucose concentration (50 or 100 g l^-1, respectively), and to reach their maximum hydrolytic activity on isoamyl acetate during the stationary growth phase. The highest ethyl acetate and isoamyl acetate concentrations in the medium were obtained with a glucose concentration of 250 g l^-1 and semianaerobic conditions.     

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     

Enhanced Asymmetric Reduction of Ethyl 3‐Oxobutyrate by Baker's Yeast via Substrate Feeding and Enzyme Inhibition

The moderate enantioselectivity of wild form baker's yeast can be considerably increased either by using continuous feeding to maintain a low substrate concentration throughout the reaction, or by the selective inhibition of competing enzymatic pathways. The reduction of ethyl 3‐oxobutyrate to ethyl (S)‐3‐hydroxybutyrate was used as a model reaction. With the substrate feeding method, the enantioselectivity could be increased from 75 % to as high as 98 %. The increased selectivity originates from the much higher substrate binding constant of the (R)‐specific enzymes, so that these enzymes remain essentially inactive if a low concentration of ethyl 3‐oxobutyrate is maintained in the bioreactor. Alternatively, the enantioselectivity of baker's yeast can be improved by selectively blocking competing enzymatic pathways. It was found that vinyl acetate is a selective inhibitor for the (R)‐specific enzymes. Ethyl (S)‐3‐hydroxybutyrate with an enantiomeric excess of 98 % was obtained by pre‐incubation of baker's yeast in 100 mM of vinyl acetate solution for 1 h. These results suggest that by selecting appropriate process conditions, natural baker's yeast can be a competitive biocatalyst for the large‐scale production of chiral secondary alcohols.     

Synthesis of polyketides from low cost substrates by the thermotolerant yeast Kluyveromyces marxianus

Kluyveromyces marxianus is a promising nonconventional yeast for biobased chemical production due to its rapid growth rate, high TCA cycle flux, and tolerance to low pH and high temperature. Unlike Saccharomyces cerevisiae, K. marxianus grows on low-cost substrates to cell densities that equal or surpass densities in glucose, which can be beneficial for utilization of lignocellulosic biomass (xylose), biofuel production waste (glycerol), and whey (lactose). We have evaluated K. marxianus for the synthesis of polyketides, using triacetic acid lactone (TAL) as the product. The 2-pyrone synthase (2-PS) was expressed on a CEN/ARS plasmid in three different strains, and the effects of temperature, carbon source, and cultivation strategy on TAL levels were determined. The highest titer was obtained in defined 1% xylose medium at 37°C, with substantial titers at 41 and 43°C. The introduction of a high-stability 2-PS mutant and a promoter substitution increased titer four-fold. 2-PS expression from a multi-copy pKD1-based plasmid improved TAL titers a further five-fold. Combining the best plasmid, promoter, and strain resulted in a TAL titer of 1.24 g/L and a yield of 0.0295 mol TAL/mol carbon for this otherwise unengineered strain in 3 ml tube culture. This is an excellent titer and yield (on xylose) before metabolic engineering or fed-batch culture relative to other hosts (on glucose), and demonstrates the promise of this rapidly growing and thermotolerant yeast species for polyketide production.     

Increase of acetate ester-hydrolysing esterase activity in mixed cultures of Saccharomyces cerevisiae and Pichia anomala

Aim: To examine the efficacy of mixed cultures with Saccharomyces cerevisiae and Pichia anomala on flavour profiles of alcoholic beverages, a Pichia mutant with low levels of ethyl acetate that negatively impact on the sensory quality was isolated. Methods and Results: A petite mutant isolated from P. anomala NBRC 10213 treated with ethidium bromide had the lower activity of ethyl acetate‐hydrolysing esterase (EAHase) than the wild‐type in crude extracts. In the fermentation tests of pure cultures, the P. anomala mutant produced less ethanol, acetate and ethyl acetate than the wild‐type. In mixed cultures with S. cerevisiae, the P. anomala mutant died quicker and produced lower amounts of ethyl acetate than the wild‐type. Mixed cultures of S. cerevisiae and P. anomala showed higher activities of EAHase than pure culture of S. cerevisiae throughout the fermentation periods. The transition to the formation of acetate esters was considerably analogous to the transition to the activity of acetate ester‐hydrolysing esterase with little time lag. Conclusions: The P. anomala mutant was superior to the wild‐type in flavour profiles. The higher ethyl acetate concentrations formed mainly by P. anomala in mixed cultures are the primary stimulus for the EAHase in S. cerevisiae and the activity of acetate ester‐hydrolysing esterase is crucial to the formation of acetate esters in mixed cultures of S. cerevisiae and P. anomala. Significance and Impact of the Study: An application of non‐Saccharomyces yeast, P. anomala to enhance the sensory quality in alcoholic beverage and a mechanism of the formation of acetate esters in mixed cultures with S. cerevisiae and P. anomala were offered.     

Acetate production from whey lactose using co-immobilized cells of homolactic and homoacetic bacteria in a fibrous-bed bioreactor

Acetate was produced from whey lactose in batch and fed-batch fermentations using co-immobilized cells of Clostridium formicoaceticum and Lactococcus lactis. The cells were immobilized in a spirally wound fibrous sheet packed in a 0.45-L column reactor, with liquid circulated through a 5-L stirred-tank fermentor. Industrial-grade nitrogen sources, including corn steep liquor, casein hydrolysate, and yeast hydrolysate, were studied as inexpensive nutrient supplements to whey permeate and acid whey. Supplementation with either 2.5% (v/v) corn steep liquor or 1.5 g/L casein hydrolysate was adequate for the cocultured fermentation. The overall acetic acid yield from lactose was 0.9 g/g, and the productivity was 0.25 g/(L h). Both lactate and acetate at high concentrations inhibited the homoacetic fermentation. To overcome these inhibitions, fed-batch fermentations were used to keep lactate concentration low and to adapt cells to high-concentration acetate. The final acetate concentration obtained in the fed-batch fermentation was 75 g/L, which was the highest acetate concentration ever produced by C. formicoaceticum. Even at this high acetate concentration, the overall productivity was 0.18 g/(L h) based on the total medium volume and 1.23 g/(L h) based on the fibrous-bed reactor volume. The cells isolated from the fibrous-bed bioreactor at the end of this study were more tolerant to acetic acid than the original culture used to seed the bioreactor, indicating that adaptation and natural selection of acetate-tolerant strains occurred. This cocultured fermentation process could be used to produce a low-cost acetate deicer from whey permeate and acid whey.     

Integrated bioprocess for enhanced production of natural flavors and fragrances by Ceratocystis moniliformis

An integrated bioprocess (IBP) for production and recovery of de novo synthesized aroma compounds was carried out by interlinking a pervaporation membrane module with a producing bioreactor. The main aroma products of the fungus Ceratocystis moniliformis were ethyl acetate, propyl acetate, isobutyl acetate, isoamyl acetate, citronellol and geraniol. In situ product removal (ISPR) using pervaporation leads to decreased product concentrations in the bioreactor and increased microbial growth rates. As a result, by circumventing inhibiting product concentrations and thus intensifying aroma production, total yield of aroma compounds produced is higher in an IBP compared with batch cultivation. In addition, permeates obtained from pervaporation consist of highly enriched mixtures of produced flavors and fragrances.