Debaryomyces hansenii fermentation for arabitol production

The fermentation process for arabitol production from glycerol was developed using a Debaryomyces hansenii strain recently selected from a broad screening. The high-producing strain produced arabitol as the only detectable polyol from glycerol. In this work, the pH, dissolved oxygen concentration (DO), inoculum size and magnesium concentration, and the nitrogen-to-phosphorus (N/P) ratio were systematically evaluated for effects on cell growth rate and arabitol productivity. Among those evaluated, the medium with N/P = 9, DO of 5% air saturation and pH 3.5 supported the highest arabitol production. Under these optimal conditions, arabitol production of 40 g/L was achieved in 5 days compared to earlier studies with 15 g/L arabitol in 5 days. Volumetric productivity and specific productivity were successfully improved from 0.13 to 0.33 g/L-h and 0.007 to 0.02 g/g-h respectively with arabitol yield of 55% from glycerol.     

Xylitol production from barley bran hydrolysates by continuous fermentation with Debaryomyces hansenii

The continuous bioconversion of xylose-containing solutions (obtained by acid hydrolysis of barley bran) into xylitol was carried out using the yeast Debaryomyces hansenii under microaerophilic conditions with or without cell recycle. In fermentations without cell recycle, the volumetric productivities ranged from 0.11–0.6 g l^–1 h^–1 were obtained for dilution rates of 0.008–0.088 h^–1. In experiments performed with cell recycle after membrane separation, the optimum xylitol productivity (2.53 g l^–1 h^–1) was reached at a dilution rate of 0.284 h^–1.     

Carbon material and bioenergetic balances of xylitol production from corncobs by Debaryomyces hansenii

The effect of oxygenation on xylitol production by the yeast Debaryomyces hansenii has been investigated in this work using the liquors from corncob hydrolysis as the fermentation medium. The concentrations of consumed substrates (glucose, xylose, arabinose, acetate and oxygen) and formed products (xylitol, arabitol, ethanol, biomass and carbon dioxide) have been used, together with those previously obtained varying the hydrolysis technique, the level of adaptation of the microorganism, the sterilization procedure and the initial substrate and biomass concentrations, in carbon material balances to evaluate the percentages of xylose consumed by the yeast for the reduction to xylitol, alcohol fermentation, respiration and cell growth. The highest xylitol concentration (71 g/L) and volumetric productivity (1.5 g/L.h) were obtained semiaerobically using detoxified hydrolyzate produced by autohydrolysis-posthydrolysis, at starting levels of xylose (S(0)) and biomass (X(0)) of about 100 g/L and 12 g(DM)/L, respectively. No less than 80% xylose was addressed to xylitol production under these conditions. The experimental data collected in this work at variable oxygen levels allowed estimating a P/O ratio of 1.16 mol(ATP)/mol(O). The overall ATP requirements for biomass production and maintenance demonstrated to remarkably increase with X(0) and for S(0) >or= 130 g/L and to reach minimum values (1.9-2.1 mol(ATP)/C-mol(DM)) just under semiaerobic conditions favoring xylitol accumulation.     

Influence of temperature and pH on xylitol production from xylose by Debaryomyces hansenii

The production of xylitol from concentrated synthetic xylose solutions (S(o) = 130-135 g/L) by Debaryomyces hansenii was investigated at different pH and temperature values. At optimum starting pH (pH(o) = 5.5), T = 24 degrees C, and relatively low starting biomass levels (0.5-0.6 g(x)/L), 88% of xylose was utilized for xylitol production, the rest being preferentially fermented to ethanol (10%). Under these conditions, nearly 70% of initial carbon was recovered as xylitol, corresponding to final xylitol concentration of 91.9 g(P)/L, product yield on substrate of 0.81 g(P)/g(S), and maximum volumetric and specific productivities of 1.86 g(P)/L x h and 1.43 g(P)/g(x) x h, respectively. At higher and lower pH(o) values, respiration also became important, consuming up to 32% of xylose, while negligible amounts were utilized for cell growth (0.8-1.8%). The same approach extended to the effect of temperature on the metabolism of this yeast at pH(o) = 5.5 and higher biomass levels (1.4-3.0 g(x)/L) revealed that, at temperatures ranging from 32-37 degrees C, xylose was nearly completely consumed to produce xylitol, reaching a maximum volumetric productivity of 4.67 g(P)/L x h at 35 degrees C. Similarly, both respiration and ethanol fermentation became significant either at higher or at lower temperatures. Finally, to elucidate the kinetic mechanisms of both xylitol production and thermal inactivation of the system, the related thermodynamic parameters were estimated from the experimental data with the Arrhenius model: activation enthalpy and entropy were 57.7 kJ/mol and -0.152 kJ/mol x K for xylitol production and 187.3 kJ/mol and 0.054 kJ/mol x K for thermal inactivation, respectively.     

Casein digestion by Debaryomyces hansenii isolated from cheese

To understand the possible proteolytic contribution of yeast during cheese ripening, Debaryomyces hansenii 212 was isolated from commercial blue-veined cheese and incubated in a medium containing casein. Growth and casein degradation were recognized at the cheese-ripening temperature. Proteolytic activity was found in the intracellular fraction, and the enzyme, which was attached to the cell wall, primarily acted on beta-casein. The cytosol contained more than 90% of the total proteolytic activity which was responsible for the degradation of both alpha(s)- and beta-casein. These results suggest that the contribution of yeast to cheese ripening would depend on the susceptibility to cell lysis in addition to its proteolytic activity.     

Casein Digestion by Debaryomyces hansenii Isolated from Cheese

To understand the possible proteolytic contribution of yeast during cheese ripening, Debaryomyces hansenii 212 was isolated from commercial blue-veined cheese and incubated in a medium containing casein. Growth and casein degradation were recognized at the cheese-ripening temperature. Proteolytic activity was found in the intracellular fraction, and the enzyme, which was attached to the cell wall, primarily acted on β-casein. The cytosol contained more than 90% of the total proteolytic activity which was responsible for the degradation of both α_s- and β-casein. These results suggest that the contribution of yeast to cheese ripening would depend on the susceptibility to cell lysis in addition to its proteolytic activity.     

汉逊德巴利酵母发酵葡萄糖生产D-阿拉伯糖醇

从378株耐高渗酵母中,筛选到1株由葡萄糖发酵高产D-阿拉伯糖醇的酵母。通过生理生化和分子生物学的鉴定,证实该菌株为Debaryomyces hansenii,保藏编号CICIM Y 0504。研究该酵母摇瓶发酵的主要影响因素,确定其摇瓶发酵条件为:葡萄糖200 g/L,酵母膏10 g/L,初始pH值3,装液量20 mL/250 mL,温度30℃。在此条件下发酵120 h,D-阿拉伯糖醇浓度达90.37 g/L,转化率45.18%。在15 L发酵罐对该酵母进行扩大培养,结果表明,初始葡萄糖浓度200 g/L的分批发酵产D-阿拉伯糖醇64.07 g/L,转化率33.94%;葡萄糖浓度控制在30～50 g/L的分批补料发酵产D-阿拉伯糖醇125 g/L,转化率37.5%。研究结果对葡萄糖发酵生产D-阿拉伯糖醇工业化的实现具有重要启示。     

表面活性剂对D-阿拉伯糖醇发酵的影响

为提高D-阿拉伯糖醇的产量,研究不同类型表面活性剂对德巴利汉逊酵母(Debaryomyces hansenii)发酵生产D-阿拉伯糖醇的影响。结果表明:阳离子和阴离子表面活性剂对D-阿拉伯糖醇的生成几乎没有影响,部分非离子表面活性剂对D-阿拉伯糖醇的生产有促进作用,其中Trition X-100的影响最为显著。在不同发酵时间加入不同浓度的Trition X-100均对D-阿拉伯糖醇的生产有促进作用,当发酵24 h添加30 g/LTrition X-100时,D-阿拉伯糖醇的产量达到最高(92.9 g/L),相比于对照增加了27.2%。     

Polygalacturonase production by Kluyveromyces marxianus: effect of medium composition

A strain of Kluyveromyces marxianus (CCT 3172), isolated from a cocoa fermentation in Brazil, secreted an endopolygalacturonase (PG) when grown under self-induced anaerobic conditions; neither polymethylesterase nor pectate lyase appeared in culture filtrates. Replacing glucose in the medium with sucrose had no effect on PG secretion or ethanol production. Growth in fructose-containing medium retarded secretion of PG and ethanol, but had no effect on growth. Growth and ethanol production in media containing galactose resembled those in fructose-containing medium, although PG secretion was lowered. Growth and PG secretion were considerably retarded in xylose-containing medium, and were similarly affected in media containing different concentrations of glucose. Varying the concentration of ammonium sulphate in media had no effect on growth or PG secretion.     

Culture parameters affecting xylitol production by Debaryomyces hansenii immobilized in alginate beads

Yeast immobilization offers operational advantages such as high cell concentration, and some drawbacks related to cell leaking and restricted mass transfer inside particles. The influence of bead size, chitosan, bead charge, volume of liquid media, and the use of corncob hydrolyzates and vinasses as culture medium were analyzed on xylitol production by Debaryomyces hansenii immobilized in alginate beads. The results showed a profuse growth of free cells, accounting 75–95% of total biomass, but electron micrographs revealed the generation of a dense biofilm with hyphal morphology at the bead surface and a very low intraparticular growth. Xylitol production was not affected by the size of particle; however chitosan had a negative effect. The use of corn cob as carbon source and twofold diluted vinasses as economic nutrients incremented xylitol concentration to 13.7 g L^?1 (Y_P/S = 0.56 g g^?1; Q_P = 0.29 g L^?1 h^?1). The best conditions corresponded to high bead charges and intermediate liquid volumes (44 g Na-alginate and 110 mL liquid medium). These results showed the feasibility of employing these cheap substrates, reflected the importance of the microaerobical conditions, and pointed to the favorable effect of cell immobilization on the metabolism of xylitol production.     

Kinetic parameters and thermodynamic values of beta-xylosidase production by Kluyveromyces marxianus

Kinetic parameters for production of beta-xylosidase by Kluyveromyces marxianus were determined in growth media containing glucose, xylose, cellobiose, sucrose and lactose as carbon sources. K. marxianus achieved maximum beta-xylosidase specific product yield (Y(P/X)) when grown on xylose. Basal level of activity was achieved in cultures grown on glucose. Kinetic parameters of enzyme production and cell mass formation were correlated. Enzyme synthesis was regulated by an induction mechanism and growth-dependent repression mechanism. Thermodynamic analysis revealed that the cell system exerted protection against thermal inactivation. A partially purified enzyme showed good stability when incubated at 60 degrees C and was quite stable at a pH of 5.0-7.0 and may be exploited for commercial applications.     

Comparative analysis of trehalose production by Debaryomyces hansenii and Saccharomyces cerevisiae under saline stress

The comparative analysis of growth, intracellular content of Na⁺ and K⁺, and the production of trehalose in the halophilic Debaryomyces hansenii and Saccharomyces cerevisiae were determined under saline stress. The yeast species were studied based on their ability to grow in the absence or presence of 0.6 or 1.0 M NaCl and KCl. D. hansenii strains grew better and accumulated more Na⁺ than S. cerevisiae under saline stress (0.6 and 1.0 M of NaCl), compared to S. cerevisiae strains under similar conditions. By two methods, we found that D. hansenii showed a higher production of trehalose, compared to S. cerevisiae; S. cerevisiae active dry yeast contained more trehalose than a regular commercial strain (S. cerevisiae La Azteca) under all conditions, except when the cells were grown in the presence of 1.0 M NaCl. In our experiments, it was found that D. hansenii accumulates more glycerol than trehalose under saline stress (2.0 and 3.0 M salts). However, under moderate NaCl stress, the cells accumulated more trehalose than glycerol. We suggest that the elevated production of trehalose in D. hansenii plays a role as reserve carbohydrate, as reported for other microorganisms.     

Utilization of salt-rich by-products from the dairy industry as feedstock for recombinant protein production by Debaryomyces hansenii

The dairy industry processes vast amounts of milk and generates high amounts of secondary by-products, which are still rich in nutrients (high Chemical Oxygen Demand (COD) and Biochemical Oxygen Demand (BOD) levels) but contain high concentrations of salt. The current European legislation only allows disposing of these effluents directly into the waterways with previous treatment, which is laborious and expensive. Therefore, as much as possible, these by-products are reutilized as animal feed material and, if not applicable, used as fertilizers adding phosphorus, potassium, nitrogen, and other nutrients to the soil. Finding biological alternatives to revalue dairy by-products is of crucial interest in order to improve the utilization of dry dairy matter and reduce the environmental impact of every litre of milk produced. Debaryomyces hansenii is a halotolerant non-conventional yeast with high potential for this purpose. It presents some beneficial traits – capacity to metabolize a variety of sugars, tolerance to high osmotic environments, resistance to extreme temperatures and pHs – that make this yeast a well-suited option to grow using complex feedstock, such as industrial waste, instead of the traditional commercial media. In this work, we study for the first time D. hansenii's ability to grow and produce a recombinant protein (YFP) from dairy saline whey by-products. Cultivations at different scales (1.5, 100 and 500 ml) were performed without neither sterilizing the medium nor using pure water. Our results conclude that D. hansenii is able to perform well and produce YFP in the aforementioned salty substrate. Interestingly, it is able to outcompete other microorganisms present in the waste without altering its cell performance or protein production capacity.     

Purification and characterization of a prolyl aminopeptidase from Debaryomyces hansenii

A prolyl aminopeptidase (PAP) (EC 3.4.11.5) was isolated from the cell extract of Debaryomyces hansenii CECT12487. The enzyme was purified by selective fractionation with protamine and ammonium sulfate, followed by two chromatography steps, which included gel filtration and anion-exchange chromatography. The PAP was purified 248-fold, with a recovery yield of 1.4%. The enzyme was active in a broad pH range (from 5 to 9.5), with pH and temperature optima at 7.5 and 45 degrees C. The molecular mass was estimated to be around 370 kDa. The presence of inhibitors of serine and aspartic proteases, bestatin, puromycin, reducing agents, chelating agents, and different cations did not have any effect on the enzyme activity. Only iodoacetate, p-chloromercuribenzoic acid, and Hg(2+), which are inhibitors of cysteine proteases, markedly reduced the enzyme activity. The K(m) for proline-7-amido-4-methylcoumarin was 40 micro M. The enzyme exclusively hydrolyzed N-terminal-proline-containing substrates. This is the first report on the identification and purification of this type of aminopeptidase in yeast, which may contribute to the scarce knowledge about D. hansenii proteases and their possible roles in meat fermentation.     

Ethanol production from Jerusalem artichoke juice using flocculent cells of Kluyveromyces marxianus

Summary Flocculent cells ofKluyveromyces marxianus SM 16-10 were used for batch production of ethanol from the inulin sugars derived from Jerusalem artichoke tubers. Using 20% initial sugar concentration, a maximum ethanol concentration of 92 g/l was achieved in 7 h, when the flocculent cell concentration was 30 g dry wt./l bioreactor volume. The same flocculent cells were used repeatedly for 7 batch runs starting with fresh medium at the beginning of each run. The ethanol yield was found to be almost constant at about 94% of the theoretical for all the 7 batch cycles, while the maximum ethanol production rate increased from 17.21 g ethanol/1/h during the first batch run to 21 g ethanol/1/h during the last batch run.     

Ethanol production from xylose is highly increased by the Kluyveromyces marxianus mutant 17694-DH1

Bioprocess and Biosystems Engineering - Directed evolutionary approach and random mutagenesis were performed on thermotolerant yeast Kluyveromyces marxianus KCTC17694 for isolating a yeast strain...     

Purification and Characterization of a Prolyl Aminopeptidase from Debaryomyces hansenii

A prolyl aminopeptidase (PAP) (EC 3.4.11.5) was isolated from the cell extract of Debaryomyces hansenii CECT12487. The enzyme was purified by selective fractionation with protamine and ammonium sulfate, followed by two chromatography steps, which included gel filtration and anion-exchange chromatography. The PAP was purified 248-fold, with a recovery yield of 1.4%. The enzyme was active in a broad pH range (from 5 to 9.5), with pH and temperature optima at 7.5 and 45°C. The molecular mass was estimated to be around 370 kDa. The presence of inhibitors of serine and aspartic proteases, bestatin, puromycin, reducing agents, chelating agents, and different cations did not have any effect on the enzyme activity. Only iodoacetate, p-chloromercuribenzoic acid, and Hg²⁺, which are inhibitors of cysteine proteases, markedly reduced the enzyme activity. The K_m for proline-7-amido-4-methylcoumarin was 40 μM. The enzyme exclusively hydrolyzed N-terminal-proline-containing substrates. This is the first report on the identification and purification of this type of aminopeptidase in yeast, which may contribute to the scarce knowledge about D. hansenii proteases and their possible roles in meat fermentation.     

马克斯克鲁维酵母的木糖和阿拉伯糖发酵

马克斯克鲁维酵母作为非常规酵母在燃料乙醇发酵中受到人们越来越多的关注。马克斯克鲁维具有天然的发酵戊糖的能力,但不同菌株的发酵能力存在较大差异。本研究比较了3株马克斯克鲁维菌株Kluyveromyces marxianus 9009/1911/1727(K.m 9009/1911/1727)在不同温度下的木糖和阿拉伯糖的发酵性能差异,结果发现不同发酵温度下,3株菌在耗糖速率、糖醇产率均表现出了显著的差异。菌株K.m 9009和K.m 1727在40℃下的发酵性能均优于30℃,这充分体现了马克斯克鲁维酵母的高温发酵优势。针对发酵差异,采用PCR方法获得3个不同菌株的戊糖代谢途径中的5种关键代谢酶(XR、XDH、XK、AR和LAD)的基因序列,并利用Clustalx 2.1进行了序列比对。结果显示3株菌的相关基因与文献中报道的1株克鲁维酵母的相应关键酶氨基酸编码序列相似性达98%以上,并且差异的氨基酸不在酶的关键位点处。在此基础上,通过Real-time实验,对木糖发酵差异最为明显的K.m 1727和K.m 1911的木糖代谢过程4个关键酶(XR、XDH、XK和ADH)的基因表达量进行测定,其结果显示对于耐热菌株K.m 1727,XDH和XK基因表达量低是导致木糖代谢过程中木糖醇积累、乙醇产量低的主要原因。最后,将所测得的马克斯克鲁维酵母的戊糖代谢关键酶序列与其他不同种属相比对,确定了其木糖和阿拉伯糖代谢途径,为进一步利用代谢工程方法提高戊糖发酵性能奠定了基础。