Identification of metabolic model: Citrate production from glucose by Candida lipolytica

The concept of mass balance was used to analyze the metabolic pathways of citrate production by Candida lipolytica from glucose. Specific rates of glucose consumption, citrate and isocitrate productions, carbon dioxide evolution, and cellular syntheses of protein and carbohydrate were observed in an NH₄⁺-limited chemostat culture. These data permitted one to assess the carbon flux in vivo by solving simultaneous carbon balance equations with respect to intermediary metabolite pools in the steady State. Among the three models considered here, model I (which coordinates the pyruvate carboxylation with the tricarboxylic acid cycle, but disregards the glyoxylate cycle) was considered plausible because the carbon flux calculated so far was acceptable. On the other hand, models II and III (which overlook the pyruvate carboxylation and the 2-oxoglutarate dehydrogenation, respectively) were found to be most unlikely because of the unusual flux assessed from these models.     

Fed-batch production of citric acid by Candida lipolytica grown on n-paraffins

This study reports on the effects of fermentor agitation and fed-batch mode of operation on citric acid production from Candida lipolytica using n-paraffin as the carbon source. An optimum range of agitation speeds in the 800-1000 rpm range corresponding to Reynolds numbers of 50000-63000 (based on initial batch conditions) seemed to give the best balance between substrate utilization for biomass growth and citric acid production. Application of multiple fed-batch feedings can be used to extend the batch fermentation and increase final citric acid concentrations and product yield. The three-cycle fed-batch system increased overall citric acid yields to 0.8-1.0 g citricacid/g n-paraffin, approximately a 100% improvement in product yield from those observed in the single cycle fed-batch system and a 200% improvement over normal batch operation. The three-cycle fed-batch mode of operation also increased the final citric acid concentration to 42 g/l from about 12 and 6g/l for single fed-batch cycle and normal batch modes of operation, respectively. Increased citric acid concentrations in three-cycle fed-batch mode was achieved at longer fermentation times.     

Oxygen uptake and citric acid production by Candida lipolytica Y 1095

The rates of oxygen uptake and oxygen transfer during cell growth and citric acid production by Candida lipolytica Y 1095 were determined. The maximum cell growth rate, 1.43 g cell/L . h, and volumetric oxygen uptake rate, 343 mg O(2)/L . h, occurred approximately 21 to 22 h after inoculation. At the time of maximum oxygen uptake, the biomass concentration was 1.3% w/v and the specific oxygen uptake rate was slightly greater than 26 mg O(2)/g cell . h. The specific oxygen uptake rate decreased to approximately 3 mg O(2)/g cell . h by the end of the growth phase.During citric acid production, as the concentration of dissolved oxygen was increased from 20% to 80% saturation, the specific oxygen uptake and specific citric acid productivity (mg citric acid/g cell . h) increased by 160% and 71%, respectively, at a biomass concentration of 3% w/v. At a biomass concentration of 5% w/v, the specific oxygen uptake and specific citric acid productivity increased by 230% and 82%, respectively, over the same range of dissolved oxygen concentrations.The effect of dissolved oxygen on citric acid yields and productivities was also determined. Citric acid yields appeared to be independent of dissolved oxygen concentration during the initial production phase; however, volumetric productivity (g citric acid/L . h) increased sharply with an increase in dissolved oxygen. During the second or subsequent production phase, citric acid yields increased by approximately 50%, but productivities decreased by roughly the same percentage due to a loss of cell viability under prolonged nitrogen-deficient conditions. (c) 1994 John Wiley & Sons, Inc.     

Optimization of citric acid production from Candida lipolytica Y-1095 using n-paraffin

Currently, the majority of worldwide microbial production of citric acid utilizes Aspergillus niger in a carbohydrate based submerged fermentation. Due to their high carbon content, hydrocarbons also have the potential of producing high concentrations of citric acid. Initial lab experiments conducted using 1875 ml batch fermentations with n-paraffin found that Candida lipolytica NRRL-Y-1095 assimilated the feedstock and had a citric acid productivity of 47 mg l(-1) h(-1). To determine the optimum level of initial biomass concentration, n-paraffin concentration, iron concentration and temperature for the production of citric acid, a central composite design was developed using 200 ml batch fermentations. The design involved conducting 31 batch fermentations under various combinations of high and low values of these four parameters. From this investigation empirical models were developed describing the interactions between the experimental parameters and citric acid production. It was found that the maximum concentration of citric acid produced was 9.8 g l(-1) and the optimum levels of each parameter for citric acid production were, 10--12% volume for initial biomass concentration, 10--15% volume for n-paraffin concentration, 10 mg l(-1) for ferric nitrate concentration, and 26--30 degrees C for temperature.     

Isolation of a bioemulsifier from Candida lipolytica

The yeast Candida lipolytica produced an inducible extracellular emulsification activity when it was grown with a number of water-immiscible carbon substrates. Negligible emulsification activity was produced by this yeast when it was grown with glucose as the carbon substrate. In hexadecane-supplemented cultures, emulsification activity was first detected after 36 h of growth, with maximum production after 130 h. A water-soluble emulsification activity was partially purified by repeated solvent extractions of the culture filtrate. This emulsifier, which we named liposan, was primarily composed of carbohydrate. Maximum emulsification activity was obtained when the ratio of hexadecane to liposan was 50:1. Maximum emulsification activity was obtained from pH 2 to 5. Liposan was heat stable to temperatures up to 70 degrees C, with a 60% loss in activity after heating for 1 h at 100 degrees C. Liposan effected stable oil-in-water emulsions with a variety of hydrocarbons.     

Citric acid production by Candida lipolytica Y 1095 in cell recycle and fed-batch fermentors

The effect of dissolved oxygen on citric acid production and oxygen uptake by Candida lipolytica Y 1095 was evaluated in cell recycle and fed-batch fermentation systems. The maximum observed volumetric productivity, which occurred at a dilution rate of 0.06 h(-1), a dissolved oxygen concentration of 80%, and a biomass concentration of 5% w/v, in the cell recycle system, was 1.32 g citric acid/L . h. At these same conditions, the citric acid yield was 0.65 g/g and the specific citric acid productivity was 24.9 mg citric acid/g cell . h. In the cell recycle system, citric acid yields ranged from 0.45 to 0.72 g/g. Both the volumetric and specific citric acid productivities were dependent on the dilution rate and the concentration of dissolved oxygen in the fermentor. Similar productivities (1.29 g citric acid/L . h) were obtained in the fed-batch system operated at a cycle time of 36 h, a dissolved oxygen concentration of 80%, and 60 g total biomass. Citric acid yields in the fed-batch fermentor were consistently lower than those obtained in the cell recycle system and ranged from 0.40 to 0.59 g/g. Although citric acid yields in the fed-batch fermentor were lower than those obtained in the cell recycle system, higher citric:isocitric acid ratios were obtained in the fed-batch fermentor. As in the cell recycle system, both the volumetric and specific citric acid productivities in the fed-batch fermentor were dependent on the cycle time and dissolved oxygen concentration. (c) 1995 John Wiley & Sons, Inc.     

Optimizing the medium components in bioemulsifiers production by Candida lipolytica with response surface method

A response surface methodology was used to study bioemulsifier production by Candida lipolytica. A 2(4) full experimental design was previously carried out to investigate the effects and interactions of the concentrations of corn oil, urea, ammonium sulfate, and potassium dihydrogen orthophosphate on the emulsification activity (EA) of the bioemulsifier produced by C. lipolytica. The best EA value (3.727 units of emulsification activity (UEA)) was obtained with a medium composed of 0.4 g of urea, 1.1 g of ammonium sulfate, 2.04 g of potassium dihydrogen orthophosphate, 5 mL of corn oil, 50 mL of distilled water, and 50 mL of seawater. A curvature check was performed and revealed a lack of fit of the linear approximation. The proximity of the optimum point was evident, as was the need for quadratic model and second-order designs that incorporate the effect of the curvature. Medium constituents were then optimized for the EA using a three-factor central composite design and response surface methodology. The second-order model showed statistical significance and predictive ability. It was found that the maximum EA produced was 4.415 UEA, and the optimum levels of urea, ammonium sulfate, and potassium dihydrogen orthophosphate were, respectively, 0.544% (m/v), 2.131% (m/v), and 2.628% (m/v).     

Mating Responses in Candida lipolytica

Culture medium that restricted cell multiplication increased fertility in selected heterothallic stocks of Candida lipolytica and triggered sporulation in newly formed diploids; a medium that supported vigorous cell growth prevented sporulation and permitted the newly formed diploids to bud.     

Fermentation of 1-hexadecene by Candida lipolytica

Candida lipolytica, strain Phaff, was grown on 1.0% 1-hexadecene as sole source of carbon. Several oxidative intermediates were isolated and identified. Based on these intermediates two pathways are proposed for the degradation of the 1-alkene via the methyl group and the double bond. Subterminal oxidation of the 1-alkene was also indicated. Cell yield, lipid content, fatty acid profile and 1, 2-diol concentration are given for various rates of aeration during growth in a fermentor.     

解脂假丝酵母(Candida lipolytica)对铜的吸附

研究了解脂假丝酵母的表面特性及培养时间、pH值、铜浓度、菌体投加量、吸附时间等因素对铜吸附的影响,并探讨了吸附动力学特征。结果表明,菌体表面可能有-OH和-PO₄^3-,培养96 h的菌体吸附性能最佳,适宜pH为4.0-6.0,适宜菌体投加量为25.0g·L^-1(湿重)。在初始浓度为20mg·L^-1的铜溶液中投加25.0g·L^-1(湿重)的菌体,吸附2h,铜的去除率最高达86.5%。铜浓度为5,10mg·L^-1时,铜的去除率高达95%以上。动力学分析表明,在实验设定的浓度范围内解脂假丝酵母对铜的吸附基本符合Freundlich吸附模型。红外光谱分析表明吸附后-OH吸收峰蓝移18cm^-1,其它吸收峰没有明显的变化。     

Sterols from Candida lipolytica yeast grown on n-alkanes

The sterols of Candida lipolytica grown on n-alkanes were isolated by reverse phase HPLC and found to be mainly ergosterol, with small quantities of ergost-7-en-3β-ol, ergosta-7,22-dien-3β-ol, ergosta-7,24(28)-dien-3β-ol and ergosta-5,7,9(11),22-tetraen-3β-ol.     

Isolation of a bioemulsifier from Candida lipolytica.

The yeast Candida lipolytica produced an inducible extracellular emulsification activity when it was grown with a number of water-immiscible carbon substrates. Negligible emulsification activity was produced by this yeast when it was grown with glucose as the carbon substrate. In hexadecane-supplemented cultures, emulsification activity was first detected after 36 h of growth, with maximum production after 130 h. A water-soluble emulsification activity was partially purified by repeated solvent extractions of the culture filtrate. This emulsifier, which we named liposan, was primarily composed of carbohydrate. Maximum emulsification activity was obtained when the ratio of hexadecane to liposan was 50:1. Maximum emulsification activity was obtained from pH 2 to 5. Liposan was heat stable to temperatures up to 70 degrees C, with a 60% loss in activity after heating for 1 h at 100 degrees C. Liposan effected stable oil-in-water emulsions with a variety of hydrocarbons.     

Production of 2-Methylisocitric Acid from n-Paraffins by Mutants of Candida lipolytica

Vitamin B₁₂-dependent ribonucleotide reductase purified from Rhizobium meliloti catalyzes the reduction of 5′-diphosphates of guanosine, adenosine, cytidine and uridine (GDP, ADP, CDP and UDP). The enzyme activities were regulated by Mg²⁺ and deoxyribonucleoside triphosphate effectors as follows: in the presence of Mg²⁺, allosteric effector deoxyguanosine triphosphate (dGTP) had the most stimulatory effect on reduction of ADP and UDP; deoxyadenosine triphosphate (dATP) on reduction of CDP; and thymidine triphosphate (dTTP) on reduction of GDP. These stimulatory effectors were active at a low concentration of 10 μm. Other deoxyribonucleotides may be negative or weakly positive effectors. Without effectors, the rate profile of ADP and GDP reduction showed a sigmoidal curve. In the absence of Mg²⁺, the activities of the reductase showed nearly maximal levels, and the addition of effectors rather decreased the activities, except in the case of UDP reduction which was most strongly stimulated by dGTP. The effect of Mg²⁺ can be replaced by Ca²⁺. Monovalent cations such as Na⁺ and K⁺ had a negligible effect on the activities of ribonucleotide reductase.     

Sequences of two tandem genes regulated by carbon sources, one being essential for n-alkane assimilation in Candida maltosa

Several n-alkane-inducible clones were isolated from the genomic library of an n-alkane-assimilation yeast, Candida maltosa, by the differential hybridization method. Among these, one of the most predominantly expressed clones was analyzed. The nucleotide sequence of the cloned DNA fragment showed that it contained two open reading frames, one encoding a protein of 127 amino acids (aa) and the other a protein of 276 aa. The former was named POX18Cm, because the sequence was highly homologous to that of the Candida tropicalis gene, POX18, which already had been identified as encoding a small oleate-inducible peroxisomal protein. The latter, named ALI1, had no homologous sequences in the EMBL database (1990 release). Northern-blot hybridization indicated that the expression of these two genes was regulated by carbon sources in the media. From gene-disruption experiments, it was concluded that ALI1 was essential for assimilation of n-alkane by C. maltosa.     

Isocitric acid production from rapeseed oil by Yarrowia lipolytica yeast

Production of d _S-threo-isocitric acid (ICA) by yeast meets serious difficulties since it is accompanied by a simultaneous production of citric acid (CA) in significant amounts that reduces the yield of desired product. In order to develop an effective process of ICA production, 60 yeast strains of different genera (Candida, Pichia, Saccharomyces, Torulopsis, and Yarrowia) were tested for their ability to produce ICA from rapeseed oil; as a result, wild-type strain Yarrowia lipolytica VKM Y-2373 and its mutant Y. lipolytica 704-UV4-A/NG50 were selected as promising ICA producers. The effects of temperature, pH, aeration, and concentrations of rapeseed oil, iron, and itaconic acid on ICA production by selected strains were studied. Under optimal conditions (pH 6.0; aeration 50–55 %; rapeseed oil concentration of 20–60 gl^?1, iron ion concentration of 1.2 mg l^?1, and itaconic acid amount of 30 mM), selected strains of Y. lipolytica produced predominantly ICA with a low amount of a by-product, CA.