Optimization of pH for high molecular weight pullulan

Summary Pullulan is a polysaccharide produced by Aureobasidium pullulans. In this study, the effect of pH on the molecular weight of pullulan was investigated. High concentration of pullulan was obtained when initial pH was 6. Pullulan having molecular weight of 500,000–600,000 was produced at initial pH of 3.0, while pullulan with molecular weight of 200,000–300,000 was produced at pH above 4.5. To obtain high molecular weight pullulan with high concentration, pH was initially controlled at pH 6, followed by pH shift from pH 6 to pH 3. Transition of pH at 2 days of fermentation was observed to be optimum. Higher molecular weight pullulan was also obtained when sucrose concentration was 50 g/l compared to the result obtained at initial sucrose concentration of 20 g/l. Sucrose concentration and pH of the fermentation broth seem to be important parameters in obtaining high molecular weight of pullulan.     

Development of Suitable Solvent System for Downstream Processing of Biopolymer Pullulan Using Response Surface Methodology

Downstream processing is an important aspect of all biotechnological processes and has significant implications on quality and yield of the final product. Several solvents were examined for their efficacy on pullulan precipitation from fermentation broth. Interactions among four selected solvents and their effect on pullulan yield were studied using response surface methodology. A polynomial model was developed using D-optimal design and three contour plots were generated by performing 20 different experiments and the model was validated by performing optimization experiments. The results indicated that lower concentration of ethanol in combination with the other three solvents has resulted in higher yield of polymer from fermentation broth and the optimized solvent system was able to recover 1.44 times more pullulan as compared to the conventional ethanolic precipitation method. These observations may help in enhancing efficiency of pullulan recovery from fermentation broth and also result in reduced cost of production for the final product.     

Downstream processing and characterization of pullulan from a novel colour variant strain of Aureobasidium pullulans FB-1

Exopolysaccharide produced by a new novel colour variant strain of Aureobasidium pullulans FB-1 was purified by cell harvesting and precipitation of the polymer. Various organic solvents were screened for pullulan precipitation. Isolation and purification of pullulan from fermentation broth was carried out using single-step purification strategy by isopropyl alcohol precipitation. Ratio of culture supernatant to isopropyl alcohol and time of precipitation were optimized for pullulan precipitation. Maximum yield (4.47%, w/v) of polysaccharide was obtained when two volumes of ice-cold isopropyl alcohol were added to one volume of supernatant with precipitation time of 12 h. IR spectra as well as carbon-13 and proton NMR spectra in aqueous solution of intact polysaccharide obtained from A. pullulans FB-1 and commercially available pullulan (Sigma, USA) revealed solely α-(1 → 6) linked maltosyl units, in accord with the generally accepted structure of pullulan. Maximum hydrolysis (94.25%) of purified pullulan at 50 °C by pullulanase was achieved under agitation (150 rpm) after 360 min.     

Effects of plastic composite support and pH profiles on pullulan production in a biofilm reactor

Pullulan is a linear homopolysaccharide which is composed of glucose units and often described as α-1, 6-linked maltotriose. The applications of pullulan range from usage as blood plasma substitutes to environmental pollution control agents. In this study, a biofilm reactor with plastic composite support (PCS) was evaluated for pullulan production using Aureobasidium pullulans. In test tube fermentations, PCS with soybean hulls, defatted soy bean flour, yeast extract, dried bovine red blood cells, and mineral salts was selected for biofilm reactor fermentation (due to its high nitrogen content, moderate nitrogen leaching rate, and high biomass attachment). Three pH profiles were later applied to evaluate their effects on pullulan production in a PCS biofilm reactor. The results demonstrated that when a constant pH at 5.0 was applied, the time course of pullulan production was advanced and the concentration of pullulan reached 32.9 g/L after 7-day cultivation, which is 1.8-fold higher than its respective suspension culture. The quality analysis demonstrated that the purity of produced pullulan was 95.8% and its viscosity was 2.4 centipoise. Fourier transform infrared spectroscopy spectra also supported the supposition that the produced exopolysaccharide was mostly pullulan. Overall, this study demonstrated that a biofilm reactor can be successfully implemented to enhance pullulan production and maintain its high purity.     

Optimization and characterization of pullulan production by a newly isolated high-yielding strain Aureobasidium melanogenum

Abstract

Pullulan is an extracellular water-soluble polysaccharide with wide applications. In this study, we screened strains that could selectively produce high molecular weight pullulan for application in industrial pullulan production. A new fungus strain A4 was isolated from soil and identified as Aureobasidium melanogenum based on colony characteristics, morphology, and internally transcribed spacer analysis. Thin-layer chromatography, Fourier-transform infrared spectroscopy, and nuclear magnetic resonance analysis suggested that the dominant exopolysaccharide produced by this strain, which presented a molecular weight of 1.384?×?10⁶ Dalton in in-gel permeation chromatography, was pullulan. The culture conditions for A. melanogenum A4 were optimized at 30?°C and 180?rpm: carbon source, 50?g/L maltose; initial pH 7; and 8?g/L Tween 80. Subsequently, batch fermentation was performed under the optimized conditions in a 5-L stirred-tank fermentor with a working volume of 3?L. The fermentation broth contained 303?g/L maltose, which produced 122.34?g/L pullulan with an average productivity of 1.0195?g/L/h and 82.32?g/L dry biomass within 120?h. The conversion efficiency of maltose to pullulan (Y%) and specific production rate (g/h/g dry cells) (Qs) reached 40.3% and 0.0251?g/L/g dry cells, respectively. The results showed strain A4 could be a good candidate for industrial production.     

AQUEOUS TWO-PHASE EXTRACTION FOR THE PURIFICATION OF ALKALINE AGARASES FROM CULTURE EXTRACTS OF Pseudomonas aeruginosa AG LSL-11

The agarases were purified for the first time an using aqueous two-phase system (ATPS) consisting of polyethylene glycol (PEG) and phosphate salt. The three extracellular, alkaline agarases produced by Pseudomonas aeruginosa AG LSL-11 were efficiently extracted into the top PEG-rich layer. The influencing factors on the partition of agarases—molecular weight of the PEG, system pH, system temperature, and NaCl concentration—were investigated. All the factors were found to have a significant effect on the partition of agarases except NaCl. The optimal ATPS parameters for the partitioning and purification of agarases were found to be 12% PEG 600 and 11.9% (w/w) phosphate salt at pH 8.0 and 4°C. All three agarases were concentrated in the top PEG phase with 6.19-fold purity and 71.21% recovery. The ATPS was found to be more convenient and economical than the conventional ion-exchange chromatography (IEC) method for extraction of three agarases and could be significantly employed for the purification of agarases from fermentation broth.     

Optimization of conditions for the production of pullulan and high molecular weight pullulan by Aureobasidium pullulans

Aureobasidium pullulans had a maximum yield coefficient of pullulan (Y _p/s=0.24) with an initial pH of the culture broth of 6.5 in a shake-flask culture. In a batch culture, the maximum pullulan yield coefficient of 0.30 was obtained at the aeration rate of 0.5 vvm. A yeast-like form and mycelial form of cells were found at the culture broth with pH controlled at 4.5 with a maximum yield coefficient of pullulan of 0.27. However, a high portion (35%) of high molecular weight pullulan (M _w>2 000 000) was produced at pH 6.5 with a yeast-like morphology of the cells.     

Pullulan: biosynthesis,production, and applications

Pullulan is a linear glucosic polysaccharide produced by the polymorphic fungus Aureobasidium pullulans, which has long been applied for various applications from food additives to environmental remediation agents. This review article presents an overview of pullulan’s chemistry, biosynthesis, applications, state-of-the-art advances in the enhancement of pullulan production through the investigations of enzyme regulations, molecular properties, cultivation parameters, and bioreactor design. The enzyme regulations are intended to illustrate the influences of metabolic pathway on pullulan production and its structural composition. Molecular properties, such as molecular weight distribution and pure pullulan content, of pullulan are crucial for pullulan applications and vary with different fermentation parameters. Studies on the effects of environmental parameters and new bioreactor design for enhancing pullulan production are getting attention. Finally, the potential applications of pullulan through chemical modification as a novel biologically active derivative are also discussed.     

普鲁兰的特性及其在食品和医学上的应用

普鲁兰是出芽短梗霉菌株分泌到胞外的一种水溶性葡聚糖。独特的联接模式赋予了普鲁兰及其衍生物与众不同的特性,具有胶粘性,成型性的同时,可以形成纤维以及很强的阻氧性等。这些性质决定了其广泛的应用价值。在介绍其结构和性质后重点论述了其在食品、生物医学以及其他工业上的应用。     

Effect of two-stage temperature on pullulan production by Aureobasidium pullulans

The effect of a two-stage cultivation temperature on the production of pullulan synthesized by Aureobasidium pullulans CGMCC1234 was investigated. Pullulan production was affected by temperature; although the optimum temperature for pullulan production was 26°C, the optimal temperature for cell growth was 32°C. Maximum pullulan production was achieved by growing A. pullulans in a first stage of 32°C for 2 days, and then in a second stage of 26°C for 2 days. Pullulan production using these two-stage temperatures significantly increased: about 27.80% (w/w) compared to constant-temperature fermentation (26°C for 4 days). The morphology of the A. pullulans (CGMCC 1234) was also affected by temperature; the lower temperature (26°C) supported unicellular biomass growth. Results of this study indicate that fermentation using two temperature stages is a promising method for pullulan production.     

Enhanced pullulan production in a biofilm reactor by using response surface methodology

Pullulan is a linear homopolysaccharide that is composed of glucose units and often described as α-1, 6-linked maltotriose. In this study, response surface methodology using Box–Behnken design was employed to study the effects of sucrose and nitrogen concentrations on pullulan production. A total of 15 experimental runs were carried out in a plastic composite support biofilm reactor. Three-dimensional response surface was generated to evaluate the effects of the factors and to obtain the optimum condition of each factor for maximum pullulan production. After 7-day fermentation with optimum condition, the pullulan production reached 60.7 g/l, which was 1.8 times higher than the result from initial medium, and was the highest yield reported to date. The quality analysis demonstrated that the purity of produced pullulan was 95.2%, and its viscosity was 2.5 centipoise (cP), which is higher than the commercial pullulan and related to its molecular weight. Fourier transform infrared spectroscopy (FTIR) also suggested that the produced exopolysaccharide was pullulan.     

Enhanced production of pigment-free pullulan by a morphogenetically arrested Aureobasidium pullulans (ATCC 42023) in a two-stage fermentation with shift from soy bean oil to sucrose

A two-stage fermentation process was established for the production of pigment-free pullulan by the yeast-like fungus Aureobasidium pullulans (ATCC 42023). In the first stage, starting at pH 4.5 with soy bean oil as the carbon source and glutamate as the nitrogen source, a cell mass of about 15 g l^–1 dry cell weight was obtained, the population being restricted mainly to the yeast form of the microorganism (yeast form more than 90% of total cells) and the formation of pigment in the culture being prevented. Small amounts of pullulan (less than 2 g l^–1) are produced at this phase, and the viscosity remained low throughout the entire growth stage. When the oil and glutamate source were nearly exhausted (below 5% of initial amounts), the cells were shifted to a production stage with sucrose as the carbon source with continued nitrogen depletion. Production of pullulan started immediately with no lag period. During 50 h of the production phase more than 35 g l^–1 of pullulan was produced (productivity approx. 0.7 g l^–1), resulting in a large increase in the viscosity of the broth. The production yield of pollulan on the sugar was about 0.6 g g^–1. Morphogenesis from the yeast form of the microorganism to chlamydospores was still restrained and no pigment was formed in the culture during the production stage. A pigment-free polysaccharide, with a molecular mass in the range of 600–750 kDa, was recovered from the supernatant of the broth after solvent precipitation.     

Optimization of physico‐chemical and nutritional parameters for a novel pullulan‐producing fungus,Eurotium chevalieri

Aims: To isolate the novel nonmelanin pullulan‐producing fungi from soil and to optimize the physico‐chemical and nutritional parameters for pullulan production. Methods and Results: A selective enrichment method was followed for the isolation, along with development of a suitable medium for pullulan production, using shake flask experiments. Pullulan content was confirmed using pure pullulan and pullulanase hydrolysate. Eurotium chevalieri was able to produce maximum pullulan (38 ± 1·0 g l^?1) at 35°C, pH 5·5, 2·5% sucrose, 0·3% ammonium sulfate and 0·2% yeast extract in a shake flash culture medium with an agitation rate of 30 rev min^?1 for 65 h. Conclusions: The novel pullulan‐producing fungus was identified as E. chevalieri (MTCC no. 9614), which was able to produce nonmelanin pullulan at from poorer carbon and nitrogen sources than Aureobasidium pullulans and may therefore be useful for the commercial production of pullulan. Significance and Impact of the Study: Eurotium chevalieri could produce pullulan in similar amounts to A. pullulans. Therefore, in future, this fungus could also be used for commercial pullulan production, because it is neither polymorphic nor melanin producing, hence its handling during pullulan fermentation will be easier and more economical.     

Pullulan production by tropical isolates of <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis>

Tropical isolates of Aureobasidium pullulans previously isolated from distinct habitats in Thailand were characterized for their capacities to produce the valuable polysaccharide, pullulan. A. pullulans strain NRM2, the so-called “color variant” strain, was the best producer, yielding 25.1 g pullulan l⁻¹ after 7 days in sucrose medium with peptone as the nitrogen source. Pullulan from strain NRM2 was less pigmented than those from the other strains and was remarkably pure after a simple ethanol precipitation. The molecular weight of pullulan from all cultures dramatically decreased after 3 days growth, as analyzed by high performance size exclusion chromatography. Alpha-amylase with apparent activity against pullulan was expressed constitutively in sucrose-grown cultures and induced in starch-grown cultures. When the alpha-amylase inhibitor acarbose was added to the culture medium, pullulan of slightly higher molecular weight was obtained from late cultures, supporting the notion that alpha-amylase plays a role in the reduction of the molecular weight of pullulan during the production phase.Names are necessary to report factually on available data; however, the USDA neither guarantees nor warrants the standard of the product, and the use of the name by the USDA implies no approval of the product to the exclusion of others that may also be suitable.     

Discovering the role of the apolipoprotein gene and the genes in the putative pullulan biosynthesis pathway on the synthesis of pullulan,heavy oil and melanin in <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis>

Pullulan produced by Aureobasidium pullulans presents various applications in food manufacturing and pharmaceutical industry. However, the pullulan biosynthesis mechanism remains unclear. This work proposed a pathway suggesting that heavy oil and melanin may correlate with pullulan production. The effects of overexpression or deletion of genes encoding apolipoprotein, UDPG-pyrophosphorylase, glucosyltransferase, and α-phosphoglucose mutase on the production of pullulan, heavy oil, and melanin were examined. Pullulan production increased by 16.93 and 8.52% with the overexpression of UDPG-pyrophosphorylase and apolipoprotein genes, respectively. Nevertheless, the overexpression or deletion of other genes exerted little effect on pullulan biosynthesis. Heavy oil production increased by 146.30, 64.81, and 33.33% with the overexpression of UDPG-pyrophosphorylase, α-phosphoglucose mutase, and apolipoprotein genes, respectively. Furthermore, the syntheses of pullulan, heavy oil, and melanin can compete with one another. This work may provide new guidance to improve the production of pullulan, heavy oil, and melanin through genetic approach.     

Aqueous two-phase extraction for the purification of alkaline agarases from culture extracts of Pseudomonas aeruginosa AG LSL-11

The agarases were purified for the first time an using aqueous two-phase system (ATPS) consisting of polyethylene glycol (PEG) and phosphate salt. The three extracellular, alkaline agarases produced by Pseudomonas aeruginosa AG LSL-11 were efficiently extracted into the top PEG-rich layer. The influencing factors on the partition of agarases--molecular weight of the PEG, system pH, system temperature, and NaCl concentration--were investigated. All the factors were found to have a significant effect on the partition of agarases except NaCl. The optimal ATPS parameters for the partitioning and purification of agarases were found to be 12% PEG 600 and 11.9% (w/w) phosphate salt at pH 8.0 and 4°C. All three agarases were concentrated in the top PEG phase with 6.19-fold purity and 71.21% recovery. The ATPS was found to be more convenient and economical than the conventional ion-exchange chromatography (IEC) method for extraction of three agarases and could be significantly employed for the purification of agarases from fermentation broth.     

Production of high molecular weight pullulan by Aureobasidium pullulans using glucosamine

Pullulan productivity was optimized in Aureobasidium pullulans ATCC 42023 with 54 g glucose l^–1. Pullulan with its higher molecular weight (>1000000) was produced using 2% (w/v) glucose and 3% (w/v) glucosamine together. The maximum concentration of pullulan was 8 g l^–1 at 140 h with shake-flask culture.     

Purification of Xylitol from Fermented Hemicellulosic Hydrolyzate Using Liquid–Liquid Extraction and Precipitation Techniques

Xylitol was produced by Candida guilliermondii by fermentation of sugarcane bagasse hemicellulosic hydrolysate. Undesirable impurities were extracted from the broth using either ethyl acetate, chloroform or dichloromethane. The best results on clarification of the broth without xylitol loss were obtained with ethyl acetate. When ethanol, acetone or tetrahydrofuran were used for precipitation of impurities, only tetrahydrofuran clarified the fermented broth, but a high xylitol loss (~30%) was observed.     

Enantioseparation of Racemic Flurbiprofen by Aqueous Two‐Phase Extraction With Binary Chiral Selectors of L‐dioctyl Tartrate and L‐tryptophan

A novel method for chiral separation of flurbiprofen enantiomers was developed using aqueous two‐phase extraction (ATPE) coupled with biphasic recognition chiral extraction (BRCE). An aqueous two‐phase system (ATPS) was used as an extracting solvent which was composed of ethanol (35.0% w/w) and ammonium sulfate (18.0% w/w). The chiral selectors in ATPS for BRCE consideration were L‐dioctyl tartrate and L‐tryptophan, which were screened from amino acids, β‐cyclodextrin derivatives, and L‐tartrate esters. Factors such as the amounts of L‐dioctyl tartrate and L‐tryptophan, pH, flurbiprofen concentration, and the operation temperature were investigated in terms of chiral separation of flurbiprofen enantiomers. The optimum conditions were as follows: L‐dioctyl tartrate, 80 mg; L‐tryptophan, 40 mg; pH, 4.0; flurbiprofen concentration, 0.10 mmol/L; and temperature, 25 °C. The maximum separation factor α for flurbiprofen enantiomers could reach 2.34. The mechanism of chiral separation of flurbiprofen enantiomers is discussed and studied. The results showed that synergistic extraction has been established by L‐dioctyl tartrate and L‐tryptophan, which enantioselectively recognized R‐ and S‐enantiomers in top and bottom phases, respectively. Compared to conventional liquid–liquid extraction, ATPE coupled with BRCE possessed higher separation efficiency and enantioselectivity without the use of any other organic solvents. The proposed method is a potential and powerful alternative to conventional extraction for separation of various enantiomers. Chirality 27:650–657, 2015. © 2015 Wiley Periodicals, Inc.     

Extraction of tetracycline from fermentation broth using aqueous two-phase systems composed of polyethylene glycol and cholinium-based salts

Aiming at developing not only cheaper but also biocompatible and sustainable extraction and purification processes for antibiotics, in this work it was evaluated the ability of aqueous two-phase systems (ATPS) composed of polyethylene glycol (PEG) and cholinium-based salts to extract tetracycline from the fermented broth of Streptomyces aureofaciens. Conventional polymer/salt and salt/salt ATPS were also studied for comparison purposes. The novel systems here proposed are able to extract tetracycline directly from the fermentation broth with extraction efficiencies higher than 80%. A tailored extraction ability of these systems can also be achieved, with preferential extractions either for the polymer- or salt-rich phases, and which further depend on the cholinium-based salt employed. The gathered results support the applicability of biocompatible ATPS in the extraction of antibiotics from complex matrices and can be envisaged as valuable platforms to be applied at the industrial level by pharmaceutical companies.