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.     

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.     

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.     

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.     

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).     

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.     

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.     

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.     

Comparative studies on citric acid production by Aspergillus niger and Candida lipolytica using molasses and glucose

Citric acid production by Aspergillus niger NCIM 548 and Candida lipolytica NCIM 3472 has been studied in shake culture using glucose and molasses as carbon sources. Methanol addition (3% v/v) at 40 h of fermentation enhanced the production of citric acid by Aspergillus niger whereas a reduction in citric acid production by Candida lipolytica was observed with addition of methanol. Maximum citric acid concentration of 12 kg/m³ was obtained with Aspergillus niger using molasses in the presence of methanol, while maximum citric acid concentration of 8.4 kg/m³ was obtained with Candida lipolytica using glucose without methanol. It appears that product formation by Aspergillus niger is either non-growth associated or partially growth associated depending on the substrate. Methanol addition changes the nature of product formation in case of Candida lipolytica.     

Complementation and Genetic Recombination in Candida lipolytica

Nutritional requirements were introduced into wild-type, heterothallic strains of Candida lipolytica by exposing the cells to X rays. Complementing hybrids were recovered from mixtures of the auxotrophic strains, and genetic recombination was observed in individually isolated ascospores from the hybrid strains.     

A novel osmotic pressure strategy to improve erythritol production by Yarrowia lipolytica from glycerol

Bioprocess and Biosystems Engineering - Polyethylene glycol (PEG) is polymer that was used to replace NaCl (reference media) as an osmotic stress agent for the synthesis of erythritol by the...