Monitoring growth and lipid production of new isolated oleaginous yeast Cryptococcus aerius UIMC65 on glucose and xylose cultures

Process monitoring is one of the most important factors affecting production efficiency at industrial scale bioprocesses. In the present work, Flow-cytometric analysis has been employed to monitor and determine neutral lipid cell droplets, granularity and size of the cells of the new oleaginous yeast, Cryptococcus aerius UIMC65. It has been shown that, differences of fluorescent intensity as well as side and forward scatter light properties have close correlations with the differences in lipid production by these yeast cells. The lipid content-related fluorescent intensity versus forward scatter parameter has been used to monitor and compare different subpopulations during growth phases on both glucose and xylose in batch cultures. Flow cytometric results have revealed that the observed differences in the proportion of each subpopulation were related to the specific growth phase and lipid content of the cells. The highest lipid content and lipid productivity were attained at 82.62%, 4.47 g/L (at 72 h) and 78.41%, 6.21 g/L (at 60 h) on glucose and xylose growth cultures, respectively. The highest biomass, lipid yield and biomass yield were found to be 7.92 g/L (on glucose culture, at 60 h), 20.92% (on glucose culture, at 48 h) and 50.71% (on glucose culture, at 24 h), respectively.     

Lipid production in batch and fed-batch cultures of Rhodosporidium toruloides from 5 and 6 carbon carbohydrates

ABSTRACT: BACKGROUND: Microbial lipids are a potential source of bio- or renewable diesel and the red yeast Rhodosporidium toruloides is interesting not only because it can accumulate over 50% of its dry biomass as lipid, but also because it utilises both five and six carbon carbohydrates, which are present in plant biomass hydrolysates. METHODS: R. toruloides was grown in batch and fed-batch cultures in 0.5 l bioreactors at pH 4 in chemically defined, nitrogen restricted (C/N 40 to 100) media containing glucose, xylose, arabinose, or all three carbohydrates as carbon source. Lipid was extracted from the biomass using chloroform-methanol, measured gravimetrically and analysed by GC. RESULTS: R. toruloides was grown on glucose, xylose, arabinose or mixtures of these carbohydrates in batch and fed-batch, nitrogen restricted conditions. Lipid production was most efficient with glucose (up to 25 g lipid L1, 48 to 75% lipid in the biomass, at up to 0.21 g lipid L1h1) as the sole carbon source, but high lipid concentrations were also produced from xylose (36 to 45% lipid in biomass). Lipid production was low (15-19% lipid in biomass) with arabinose as sole carbon source and was lower than expected (30% lipid in biomass) when glucose, xylose and arabinose were provided simultaneously. The presence of arabinose and/or xylose in the medium increased the proportion of palmitic and linoleic acid and reduced the proportion of oleic acid in the fatty acids, compared to glucose-grown cells. High cell densities were obtained in both batch (37 g L1, with 49% lipid in the biomass) and fed-batch (35 to 47 g L1, with 50 to 75% lipid in the biomass) cultures. The highest proportion of lipid in the biomass was observed in cultures given nitrogen during the batch phase but none with the feed. However, carbohydrate consumption was incomplete when the feed did not contain nitrogen and the highest total lipid and best substrate consumption were observed in cultures which received a constant low nitrogen supply. CONCLUSIONS: Lipid production in R. toruloides was lower from arabinose and mixed carbohydrates than from glucose or xylose. Although high biomass and lipid production were achieved in both batch and fed-batch cultures with glucose as carbon source, for lipid production from mixtures of carbohydrates fed-batch cultivation was preferable. Constant feeding was better than intermittent feeding. The feeding strategy did not affect the relative proportion of different fatty acids in the lipid, but the presence of C5 sugars did.     

Multi-parameter flow cytometry as a tool to monitor heterotrophic microalgal batch fermentations for oil production towards biodiesel

Multi-parameter flow cytometry was used to monitor cell intrinsic light scatter, viability, and lipid content of Chlorella protothecoides cells grown in shake flasks. Changes in the right angle light scatter (RALS) and forward angle light scatter (FALS) were detected during the microalgal growth, which were attributed to the different microalgal cell cycle stages. The proportion of cells not stained with PI (cells with intact cytoplasmic membrane) was high (> 90%) during the microalgal growth, even in the latter stationary phase, suggesting that the microalgal cells built-up storage materials which allowed them to survive under nutrient starvation, maintaining their cytoplasmic membranes intact. A high correlation between the Nile Red fluorescence intensity measured by flow cytometry and total lipid content assayed by the traditional lipid extraction method was found for this microalga, making this method a suitable and quick technique for the screening of microalgal strains for lipid production, optimization of biofuel production bioprocesses, and scale-up studies. The highest oil content (∼28% w/w dry cell weight, estimated by flow cytometry) was observed in the latter stationary phase. In addition, C. protothecoides oil also depicted the adequate fatty acid methyl ester composition for biodiesel purposes at this growth phase, suggesting that the microalgal oil produced during the latter stationary phase could be an adequate substitute for diesel fuel. Medium growth optimization for enhancement of microalgal oil production is now in progress, using the multi-parameter approach.     

Monitoring <Emphasis Type="Italic">Rhodosporidium toruloides</Emphasis> NCYC 921 batch fermentations growing under carbon and nitrogen limitation by flow cytometry

The yeast Rhodosporidium toruloides NCYC 921 was grown on carbon or nitrogen limited batch cultures. The fermentations were monitored using traditional techniques and multi-parameter flow cytometry. The lipid content was assessed by flow cytometry in association with the fluorocrome Nile Red which emits yellow gold fluorescence when dissolved in neutral lipids and red fluorescence when dissolved in polar lipids. In this way, it was possible to at-line monitor the yeast lipid composition in terms of polarity classes throughout the batch growths. It was found that the neutral lipids decreased during the carbon-limited stationary phase, and increased during the nitrogen-limited batch growth. The maximum lipid content was obtained for the nitrogen-limited yeast culture (24% w/w lipids). The yeast cells with permeabilised membranes profile remained almost unchanged during the time course of both fermentations. The scatter light measurements (forward and side scatter signals) provided information on the yeast growth phase. The multi-parameter flow cytometric approach here reported represents a better control system based on measurements made at the single cell level for optimization of the yeast lipid production bioprocess performance.     

糠醛对粘红酵母生长与油脂积累的影响

为了探究纤维素水解液中常见的发酵抑制物糠醛对粘红酵母Rhodotorula glutinis生长与油脂积累的影响,对比了不同的糠醛浓度(0.1、0.4、0.6、1.5 g/L)下粘红酵母的生物量和油脂积累情况,并探究了1.0 g/L的糠醛对粘红酵母不同碳源(葡萄糖和木糖)利用的影响。研究表明,当糠醛浓度达1.5 g/L时,粘红酵母的延迟期延长至96 h,残糖高达17.7 g/L,生物量最高6.6 g/L,仅为正常积累量的47%,油脂含量也减少了约50%;以木糖为碳源时,糠醛对粘红酵母的抑制程度小于葡萄糖为碳源时的情况;在糠醛存在的逆境中,粘红酵母倾向于生成更多的18碳脂肪酸或18碳不饱和脂肪酸。     

Limits of propidium iodide as a cell viability indicator for environmental bacteria.

BACKGROUND: Viability measurements of individual bacteria are applied in various scopes of research and industry using approaches where propidium iodide (PI) serves as dead cell indicator. The reliability of PI uptake as a cell viability indicator for dead (PI permeable) and viable (PI impermeable) bacteria was tested using two soil bacteria, the gram(-) Sphingomonas sp. LB126 and the gram(+) Mycobacterium frederiksbergense LB501T. METHODS: Bacterial proliferation activities observed viaDAPI and Hoechst 33342 staining were linked to the energy charge and the proportion of dead cells as obtained by diOC(6) (3)-staining and PI-uptake, respectively. Calibration and verification experiments were performed using batch cultures grown on different substrates. RESULTS: PI uptake depended on the physiological state of the bacterial cells. Unexpectedly, up to 40% of both strains were stained by PI during early exponential growth on glucose when compared to 2-5% of cells in the early stationary phase of growth. CONCLUSIONS: The results question the utility of PI as a universal indicator for the viability of (environmental) bacteria. It rather appears that in addition to nonviable cells, PI also stains growing cells of Sphingomonas sp. and M. frederiksbergense during a short period of their life cycle.     

Biosynthesis of Poly-beta-Hydroxyalkanoates from Pentoses by Pseudomonas pseudoflava

The potential of Pseudomonas pseudoflava to produce poly-beta-hydroxyalkanoates (PHAs) from pentoses was studied. This organism was able to use a hydrolysate from the hemicellulosic fraction of poplar wood as a carbon and energy source for its growth. However, in batch cultures, growth was inhibited completely at hydrolysate concentrations higher than 30% (vol/vol). When P. pseudoflava was grown on the major sugars present in hemicelluloses in batch cultures, poly-beta-hydroxybutyric acid (PHB) accumulated when glucose, xylose, or arabinose was the sole carbon source, with the final PHB content varying from 17% (wt/wt) of the biomass dry weight on arabinose to 22% (wt/wt) of the biomass dry weight on glucose and xylose. Specific growth rates were 0.58 h on glucose, 0.13 h on xylose, and 0.10 h on arabinose, while the specific PHB production rates based on total biomass ranged from 0.02 g g h on arabinose to 0.11 g g h on glucose. PHB weight-average molecular weights were 640,000 on arabinose and 1,100,000 on glucose and xylose. The absolute amount of PHB in the cells decreased markedly when nitrogen limitation was relaxed by feeding ammonium sulfate at the end of the PHB accumulation stage of the arabinose and xylose fermentations. Copolymers of beta-hydroxybutyric and beta-hydroxyvaleric acids were produced when propionic acid was added to shake flasks containing 10 g of glucose liter. The beta-hydroxyvaleric acid monomer content attained a maximum of 45 mol% when the initial propionic acid concentration was 2 g liter.     

Glucose repression of xylose utilisation by Lactococcus lactisIO-1

In dual substrate (5 g glucose l , 5 g xylose l ) batch fermentation of L. lactis IO-1 a classic diauxie was observed. In batch fermentations (5 g xylose l ) xylose isomerase activity was only detected in xylose grown cells. In mixed-substrate, carbon limited chemostat cultures (5 g glucose l , 5 g xylose l ) xylose utilisation was partially repressed by glucose at dilution rates above 0.01 h and completely repressed at 0.50 h .     

耐乙酸粘红酵母合成油脂

乙酸是木质纤维素在水解过程中的主要副产物,高浓度的乙酸严重影响产油微生物的生长和油脂合成。本文研究了粘红酵母对乙酸的耐受性及其利用乙酸合成微生物油脂的能力。结果表明,在初始葡萄糖、木糖浓度分别为6 g/L和44 g/L的混合糖培养基中,乙酸浓度低于10 g/L时,不会对菌体生长产生抑制作用,油脂合成还得到了促进。当乙酸添加量为10 g/L时,生物量、油脂产量、油脂含量较对照组分别提高了21.5%、171.2%和121.6%。进一步研究表明,粘红酵母具备利用乙酸合成油脂的能力,当以乙酸为唯一碳源,浓度为25 g/L时,油脂产量达到3.20 g/L,油脂质量得率为13%。微生物油脂成分分析表明,粘红酵母以乙酸为底物制得的油脂可以作为制备生物柴油的油脂原料,其主要成分为棕榈酸、硬脂酸、油酸、亚油酸和亚麻酸,其中饱和脂肪酸和不饱和脂肪酸含量分别为40.9%和59.1%。由于粘红酵母具有利用乙酸合成微生物油脂的能力,在以木质纤维素水解液为原料生产微生物油脂的脱毒过程中,一定浓度的乙酸可以不必脱除。     

Production of β-carotene by a mutant of Rhodotorula glutinis

Wild strains of Rhodotorula glutinis and R. rubra were investigated concerning their carotenoid production, proportion of beta-carotene and cell mass yield. R. glutinis NCIM 3353 produced 2.2 mg carotenoid/l in 72 h; and the amount of beta-carotene was 14% (w/w) of the total carotenoid content (17 microg/g cell dry weight). It was subjected to mutagenesis using UV radiation for strain improvement. Out of 2,051 isolates screened, the yellow coloured mutant 32 produced 120-fold more beta-carotene (2,048 microg/g cell dry weight) than the parent culture in 36 h, which was 82% (w/w) of the total carotenoid content. Mutant 32 was grown on different carbon and nitrogen sources. The best yield of beta-carotene (33+/-3 mg/l) was obtained when glucose and yeast extract were supplied as carbon and nitrogen sources, respectively. Divalent cation salts further increased the total carotenoid content (66+/-2 mg/l) with beta-carotene as the major component (55+/-2%, w/w).     

Lipid Cytochemistry and Morphologic Change in Aging Populations of Tetrahymena

SYNOPSIS. In cultures of strains GL, S, W, and WH6 of Tetrahymena pyriformis grown in proteose-peptone medium and stained with phosphine 3R the percentage of cells containing lipid granules increased in early stationary phase, decreased in the middle of stationary phase, and increased again toward the end of culture life. Granules appeared first in the anterior ends of cells and spread thruout the cytoplasm as the cultures aged. These granules consisted of neutral fat and were present in living cells. Changes in lipid accumulation were correlated with changes in cellular size, shape, volume and fragility.     

The kinetics of end-product inhibition of l-lactate production from xylose and glucose by Lactococcus lactis IO-1

Summary The relative contributions of lactate inhibition and the generation of sterile (undividing) cells to the low xylose utilisation rate of Lactococcus lactis IO-1 was investigated. The lactate inhibition constant of xylose grown cells was shown to be 9.3 times more than that of glucose grown cells. However, the sterile cell production rate and LDH inactivation rate of the xylose cultures were at least 10 times less than the glucose cultures. Thus, it is suggested that the slower substrate consumption rate in xylose medium is caused mainly by the large inhibition constant for the end product.     

Xylose induced decrease in hexokinase PII activity confers resistance to carbon catabolite repression of invertase synthesis in Saccharomyces carlsbergensis

The relationship between the xylose induced decrease in hexokinase PII activity and the derepression of invertase synthesis in yeast is described. When xylose was added to cells growing in a chemostat under nitrogen limitation, the catabolic repression was supressed as shown by the large increase on invertase levels even if glucose remained high. The glucose phosphorylating-enzymes were separated by hydroxylapatite chromatography and it is shown that the treatment with xylose is accompanied by a loss of 98% hexokinase PII and a 50% of the PI isoenzyme, whereas the levels of glucokinase as well as those of glucose-6-phosphate, fructose-6-phosphate, pyruvate and ATP remained unaffected.The analysis of the enzymes present in cells grown in ethanol, limiting glucose and high glucose, shows that hexokinase PII predominates in cells under catabolic repression, the opposite is true for glucokinase, whereas hexokinase PI remains unaffected.     

Corecovery of lipids and fermentable sugars from Rhodosporidium toruloides using ionic liquid cosolvents: Application of recycle to batch fermentation

This work evaluates the ability of an ionic liquid‐methanol cosolvent system to extract lipids and recycle fermentable sugars recovered from oil‐bearing Rhodosporidium toruloides grown in batch culture on defined media using glucose and xylose as carbon sources. Growth on the recycled mixed carbon substrate was successful with glucose consumed before xylose and overall cell mass to lipid yields (Y_P/X) between 57% and 61% (w/w relative to whole dried cell mass) achieved. Enzymatic hydrolysis of the delipified carbohydrate fraction recovered approximately 9%–11% (w/w) of the whole dried cell mass as fermentable sugars, which were successfully recycled as carbon sources without further purification. In total, up to 70% (w/w) of the whole dried cell mass was recovered as lipids and fermentable sugars and the substrate to lipid yields (Y_P/S) was increased from 0.12 to 0.16 g lipid/g carbohydrate consumed, highlighting the promise of this approach to process lipid bearing cell biomass. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1239–1242, 2014     

Enhancement of chemotaxis in Spirochaeta aurantia grown under conditions of nutrient limitation.

Spirochaeta aurantia M1 cells were grown in a chemostat under conditions of energy and carbon source limitation. The chemotactic responses of the chemostat-grown cells were compared with those of S. aurantia cells grown in batch culture in the presence of excess energy and carbon source. Chemotactic responses were measured by determining the number of cells that entered a capillary tube containing a solution of attractant. S. aurantia cells grown in the chemostat under energy and carbon source limitation exhibited enhanced chemotactic responses and detected lower concentrations of attractant, as compared with cells grown in batch culture. The chemotactic response toward an attractant was specifically enhanced when that attractant was the growth-limiting energy and carbon source. The medium used contained either D-glucose or D-xylose as the sole energy and carbon source. Cells had the greatest chemotactic response toward glucose when grown at a dilution rate (D) of 0.045 h-1 under glucose limitation and toward xylose when grown at D = 0.06 h-1 under xylose limitation. When cells were grown under glucose limitation (D = 0.045 h-1), they sensed concentrations of attractant (glucose) ca. 1,000 times lower than those sensed by batch-grown cells. A similar enhancement of sensing ability (toward xylose) was observed in cells grown under xylose limitation. The results indicated that S. aurantia cells are able to regulate their chemosensory system in response to nutrient limitation. Maximum enhancement of chemotaxis occurs in cells growing at very low concentrations of energy and carbon source. Most likely, this property provides the spirochetes with competitive advantages when the availability of nutrients becomes severely limited in their habitats.     

The effect of glycerol as a sole and secondary substrate on the growth and fatty acid composition of Rhodotorula glutinis

Rhodotorula glutinis is a yeast that produces copious quantities of lipids in the form of triacylglycerols (TAG) and can be used to make biodiesel via a transesterification process. The ester bonds in the TAG are broken leaving behind two products: fatty acid methyl esters and glycerol that could provide an inexpensive carbon source to grow oleaginous yeast R. glutinis. Described here are the effects of different growth substrates on TAG accumulation and fatty acids produced by R. glutinis. Yeast cultured 24h on medium containing dextrose, xylose, glycerol, dextrose and xylose, xylose and glycerol, or dextrose and glycerol accumulated 16, 12, 25, 10, 21, and 34% TAG on a dry weight basis, respectively. Lipids were extracted from R. glutinis culture and transesterified to form fatty acid methyl esters. The results show a difference in the degree of saturation for the carbon sources tested. Cells cultivated on glycerol alone had the highest degree of unsaturated fatty acids at 53% while xylose had the lowest at 25%. R. glutinis can be cultivated on all sugars tested as single carbon substrates or in mixtures. Glycerol may be used as secondary or primary carbon substrate.     

Accumulation of docosahexaenoic acid-rich lipid in thraustochytrid <Emphasis Type="Italic">Aurantiochytrium</Emphasis> sp. strain T66: effects of N and P starvation and O<Subscript>2</Subscript> limitation

Aurantiochytrium sp. strain T66 was grown in batch bioreactor cultures in a defined glutamate- and glycerol-containing growth medium. Exponentially growing cells had a lipid content of 13% (w/w) of dry weight. A fattening of cells fed excess glycerol occurred in the post-exponential growth phase, after the medium was depleted of N or P. Lipid accumulation was also initiated by O(2) limitation (below 1% of saturation). N starvation per se, or in combination with O(2) limitation, gave the highest lipid content, i.e., 54% to 63% (w/w) of dry weight. The corresponding maximum culture density was 90 to 100 g/l dry biomass. The content of docosahexaenoic acid (22:6n-3) in N starved, well-oxygenated cells reached 29% (w/w) of total fatty acids but increased to 36% to 52% in O(2)-limited cells, depending on the time span of the limitation. O(2)-limited cells did not accumulate the monounsaturated fatty acids that were normally present. We inferred that the biological explanation is that O(2) limitation hindered the O(2)-dependent desaturase(s) and favored the O(2)-independent polyunsaturated fatty acid synthase. The highest overall volumetric productivity of docosahexaenoic acid observed was 93 mg/l/h. Additionally, we present a protocol for quantitative lipid extraction, involving heat and protease treatment of freeze-dried thraustochytrids.     

Enhancement of (R,R)-2,3-butanediol production from xylose by Paenibacillus polymyxa at elevated temperatures

Conversion of xylose to (R,R)-2,3-butanediol by Paenibacillus polymyxa in anaerobic batch and continuous cultures was increased by 39% and 52%, respectively, by increasing the growth temperatures from 30 to 39 °C. There was no effect of temperature when glucose was used as substrate. 39 mM (R,R)-2,3-butanediol, 65 mM ethanol, and 47 mM acetate were obtained from 100 mM xylose after 24 h batch culture at 39 °C. With 100 mM glucose and 100 mM xylose used together in a batch culture at 39 °C, all xylose was consumed after 24 h and 82 mM (R,R)-2,3-butanediol, 124 mM ethanol and 33 mM acetate were produced.     

Biosynthesis of Poly-β-Hydroxyalkanoates from Pentoses by Pseudomonas pseudoflava

The potential of Pseudomonas pseudoflava to produce poly-β-hydroxyalkanoates (PHAs) from pentoses was studied. This organism was able to use a hydrolysate from the hemicellulosic fraction of poplar wood as a carbon and energy source for its growth. However, in batch cultures, growth was inhibited completely at hydrolysate concentrations higher than 30% (vol/vol). When P. pseudoflava was grown on the major sugars present in hemicelluloses in batch cultures, poly-β-hydroxybutyric acid (PHB) accumulated when glucose, xylose, or arabinose was the sole carbon source, with the final PHB content varying from 17% (wt/wt) of the biomass dry weight on arabinose to 22% (wt/wt) of the biomass dry weight on glucose and xylose. Specific growth rates were 0.58 h⁻¹ on glucose, 0.13 h⁻¹ on xylose, and 0.10 h⁻¹ on arabinose, while the specific PHB production rates based on total biomass ranged from 0.02 g g⁻¹ h⁻¹ on arabinose to 0.11 g g⁻¹ h⁻¹ on glucose. PHB weight-average molecular weights were 640,000 on arabinose and 1,100,000 on glucose and xylose. The absolute amount of PHB in the cells decreased markedly when nitrogen limitation was relaxed by feeding ammonium sulfate at the end of the PHB accumulation stage of the arabinose and xylose fermentations. Copolymers of β-hydroxybutyric and β-hydroxyvaleric acids were produced when propionic acid was added to shake flasks containing 10 g of glucose liter⁻¹. The β-hydroxyvaleric acid monomer content attained a maximum of 45 mol% when the initial propionic acid concentration was 2 g liter⁻¹.